INCENDIO

PROGETTAZIONE STRUTTURALE ANTINCENDIO
A.A. 2022/23:
caratteristiche dell’azione incendio
Prof. Ing. Franco Bontempi
Docente di TEORIA E PROGETTO DI PONTI – GESTIONE DI PONTI E GRANDI STRUTTURE –
PROGETTAZIONE STRUTTURALE ANTINCENDIO
Facoltà di Ingegneria Civile e Industriale
Università degli Studi di Roma La Sapienza
franco.bontempi@uniroma1.it

DEFINIZIONE DI INCENDIO
•Incendio = combustione autoalimentata ed incontrollata
di materiali combustibili.
• I PARTE: Carattere estensivo (diffusione nello spazio):
1. wildfire
2. urbanfire
3. all’esterno di un edificio
4. all’interno di un interno
• II PARTE: Carattere intensivo (andamento nel tempo).
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• Carattere estensivo (diffusione nello spazio):
1. wildfire
2. urbanfire
• Carattere intensivo (andamento nel tempo).

CARATTERE ESTENSIVO
I

1. WILDFIRE

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http://www.meteoweb.eu/2012/06/reggio-
calabria-vasto-incendio-distrugge-la-collina-
di-pentimele-oasi-ridosso-della-citta/140184/
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http://www.repubblica.it/esteri/2014/04/13/
foto/cile_gigantesco_incendio_a_valparaiso_3
mila_evacuati-83468928/1/#1
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RUNAWAY (1)
effect
time 29

EFFECT
RUNAWAY
(2)
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2. URBANFIRE

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The Great Fire of London 2 September - 5 September 1666.
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The Great Fire of the City of New York, 16 December 1835
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The Great Fire of Chicago, October 7-10, 1871
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https://it.wikipedia.org/wiki/Terr
emoto_di_San_Francisco_del_190
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https://it.wikipedia.org/wiki/Gran
de_terremoto_del_Kant%C5%8D_
del_1923
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https://it.wikipedia.org/wiki/Grande_terremoto_del_Kant%C5%8D_del_1923
• Il terremoto devastò Tokyo, il porto di Yokohama, e le prefetture circostanti
di Chiba, Kanagawa, e Shizuoka, e causò grandi distruzioni in tutta la regione
del Kantō. Le morti causate dal sisma sono stimate fra 100.000 e 142.000,
mentre i dispersi, presumibilmente deceduti, furono 37.000.
• Dato che il terremoto avvenne all'ora di pranzo, quando molte persone
stavano utilizzando il fuoco per cucinare, i danni furono incrementati da
incendi che divamparono in numerosi luoghi e che furono rapidamente
alimentati dal violento tifone che si stava avvicinando dalla costa della
penisola di Noto nel nord del Giappone.
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https://it.wikipedia.org/wiki/Grande_terremoto_del_Kant%C5%8D_del_1923
• Gli incendi provocarono la fusione dell'asfalto delle strade, intrappolando ed
uccidendo molte persone che tentavano la fuga. L'episodio singolo che vide il
più grande numero di morti fu l'incenerimento in un vortice di fuoco di circa
38.000 persone radunate in uno spazio aperto a Rikugun Honjo Hifukusho a
Tokyo e che credevano di essere ormai in salvo.
• Il terremoto provocò la rottura delle falde acquatiche, rendendo più difficili
lo spegnimento dei fuochi, che durarono due giorni, fino alla mattina del 3
settembre, quando si spensero per mancanza di combustibile. Gli incendi
furono la principale causa del grande numero di vittime.
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Cascade Effect / Chain Reaction
• A cascade effect is an inevitable and sometimes unforeseen chain
of events due to an act affecting a system.
• In biology, the term cascade refers to a process that, once started,
proceeds stepwise to its full, seemingly inevitable, conclusion.
• A chain reaction is the cumulative effect produced when one
event sets off a chain of similar events.
• It typically refers to a linked sequence of events where the time
between successive events is relatively small.
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effect
time
decomposability
course predictability
Runaway

3. ALL’ESTERNO DI UN EDIFICIO

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Bad vs Good Collapse
STRUCTURE
& LOADS
Collapse
Mechanism
NO SWAY
“IMPLOSION”
OF THE
STRUCTURE
“EXPLOSION”
OF THE
STRUCTURE
is a process in which
objects are destroyed by
collapsing on themselves
is a process
NOT CONFINED
SWAY

4. ALL’INTERNO DI UN EDIFICIO

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Finite Volume Discretization

Two zone discretization

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www.francobontempi.or
g
Str
o N
GER
www.stronger2012.com
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NUMERICAL
MODELING
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Description of Enclosure Fires

Pre-flashover fire
• The growth stage of a fire, where the emphasis in fire safety engineering
design is on the safety of humans.
• The design load is in this case characterized by an energy release rate curve,
where the growth phase of the fire is of most importance.

Flashover
• The transition from the fire growth period to the fully developed stage in the
enclosure fire development.
• The formal definition from the International Standards Organization is “the
rapid transition to a state of total surface involvement in a fire of
combustible material within an enclosure.”
• In fire safety engineering the word is used to indicate the demarcation point
between two stages of a compartment fire, i.e., pre-flashover and post-
flashover.

Post-flashover fire
• When the objective of fire safety engineering design is to ensure structural
stability and safety of fire fighters, the post-flashover fire is of greatest
concern.
• The design load in this case is characterized by the temperature–time curve
assumed for the fully developed fire stage.

Fuel-controlled fire
• After ignition and during the initial fire growth stage, the fire is said to be
fuel-controlled, since in the initial stages there is sufficient oxygen available
for combustion and the growth of the fire entirely depends on the
characteristics of the fuel and its geometry.
• The fire can also be fuel-controlled in later stages.

Ventilation-controlled fire
• As the fire grows it may become ventilation-controlled, when there is not
enough oxygen available to combust most of the pyrolyzing fuel.
• The energy release rate of the fire is then determined by the amount of
oxygen that enters the enclosure openings.

Fully developed fire
• Synonymous with the post-flashover fire, which lasts from the occurrence of
flashover through the decay stage to extinction.
• During most of this period the fire is ventilation-controlled; at some point
during the decay period it becomes fuel controlled again.

Backdraft
• Limited ventilation during an enclosure fire can lead to the production of
large amounts of unburnt gases. When an opening is suddenly introduced,
the inflowing air may mix with these, creating a combustible mixture of
gases in some part of the enclosure.
• Any ignition sources, such as a glowing ember, can ignite this flammable
mixture, resulting in an extremely rapid burning of the gases. Expansion due
to the heat created by the combustion will expel the burning gases out
through the opening and cause a fireball outside the enclosure.
• The phenomenon can be extremely hazardous.

Interactions
• Fire is a physical and chemical phenomenon that is strongly interactive by
nature. The interactions between the flame, its fuel, and the surroundings
can be strongly nonlinear, and quantitative estimation of the processes
involved is often complex.
• The processes of interest in an enclosure fire mainly involve mass fluxes and
heat fluxes to and from the fuel and the surroundings.
• Figure shows a schematic of these interactions, indicating the complexity of
the mass and heat transfer processes occurring in an enclosure fire.

Schematic of the heat fluxes and mass fluxes occurring in an enclosure fire.

Processes
• The processes occurring in the flame involve the flow of energy and the flow
of mass.
• The flow of energy occurs by the processes of radiation, convection, and
conduction.
• The dominant process is that of radiation; it is mainly the soot particles
produced by combustion that glow and radiate heat in all directions. The
radiation down toward the solid is the main heat transfer mode, which melts
the solid, but convection also plays a role.
• The convective heat flux is mainly upward, transferring heat up and away
from the combustion zone. The larger and more luminous the flame, the
quicker the melting process.

Ignition
• After ignition, the fire grows and produces increasing amounts of energy,
mostly due to flame spread. In the early stages the enclosure has no effect
on the fire, which then is fuel controlled.
• Besides releasing energy, a variety of toxic and nontoxic gases and solids are
produced.
• The generation of energy and combustion products is a very complex issue,
as mentioned above, and the engineer must rely on measurements and
approximate methods in order to estimate energy release rates and the yield
of combustion products.

Development and descent of a hot smoke layer.

Plume
• The hot gases in the flame are surrounded by cold gases, and the hotter, less
dense mass will rise upward due to the density difference, or rather, due to
buoyancy. The buoyant flow, including any flames, is referred to as a fire
plume.
• As the hot gases rise, cold air will be entrained into the plume. This mixture
of combustion products and air will impinge on the ceiling of the fire
compartment and cause a layer of hot gases to be formed.
• Only a small portion of the mass impinging on the ceiling originates from the
fuel; the greatest portion of this mass originates from the cool air entrained
laterally into the plume as it continues to move the gases toward the ceiling.
• As a result of this entrainment, the total mass flow in the plume increases,
and the average temperature and concentration of combustion products
decreases with height.

Ceiling jet
• When the plume flow impinges on the ceiling, the gases spread across it as a
momentum-driven circular jet. The velocity and temperature of this jet is of
importance, since quantitative knowledge of these variables will allow
estimates to be made on the response of any smoke and heat detectors and
sprinkler links in the vicinity of the ceiling.
• The ceiling jet eventually reaches the walls of the enclosure and is forced to
move downward along the wall.
• However, the gases in the jet are still warmer than the surrounding ambient
air, and the flow will turn upward due to buoyancy. A layer of hot gases will
thus be formed under the ceiling.

Gas temperatures
• Experiments have shown, for a wide range of compartment fires, that it is
reasonable to assume that the room becomes divided into two distinct
layers:
I. a hot upper layer consisting of a mixture of combustion products and
entrained air, and
II. a cold lower layer consisting of air.
• Further, the properties of the gases in each layer change with time but are
assumed to be uniform throughout each layer. For example, it is commonly
assumed when using engineering methods that the temperature is the same
throughout the hot layer at any given time.

Finite Volume Discretization

Two zone discretization

The hot layer
• The plume continues to entrain air from the lower layer and transport it
toward the ceiling. The hot upper layer therefore grows in volume, and the
layer interface descends toward the floor.

Heat transfer
• As the hot layer descends and increases in temperature, the heat transfer
processes are augmented. Heat is transferred by radiation and convection
from the hot gas layer to the ceiling and walls that are in contact with the
hot gases. Heat from the hot layer is also radiated toward the floor and the
lower walls, and some of the heat will be absorbed by the air in the lower
layer.
• Additionally, heat is transferred to the fuel bed, not only by the flame but to
an increasing extent by radiation from the hot layer and the hot enclosure
boundaries.
• This leads to an increase in the burning rate of the fuel and the heating up of
other fuel packages in the enclosure.

Vent flows
• If there is an opening to the adjacent room or out to the atmosphere, the
smoke will flow out through it as soon as the hot layer reaches the top of the
opening.
• Often, the increasing heat in the enclosure will cause the breakage of
windows and thereby create an opening.

Flashover
• The fire may continue to grow, either by increased burning rate, by flame
spread over the first ignited item, or by ignition of secondary fuel packages.
The upper layer increases in temperature and may become very hot.
• As a result of radiation from the hot layer toward other combustible material
in the enclosure, there may be a stage where all the combustible material in
the enclosure is ignited, with a very rapid increase in energy release rates.
• This very rapid and sudden transition from a growing fire to a fully
developed fire is called flashover.

Smoke gas explosion
• When unburnt gases from an under ventilated fire flow through leakages
into a closed space connected to the fire room, the gases there can mix very
well with air to form a combustible gas mixture.
• A small spark is then enough to cause a smoke gas explosion, which can have
very serious consequences.
• This phenomenon is, however, very seldom observed in enclosure fires.

Stages in enclosure fire development

Ignition
• Ignition can be considered as a process that produces an exothermic
reaction characterized by an increase in temperature greatly above the
ambient.
• It can occur either by piloted ignition (by flaming match, spark, or another
pilot source) or by spontaneous ignition (through accumulation of heat in
the fuel).
• The accompanying combustion process can be either flaming combustion or
smoldering combustion.

Growth
• Following ignition, the fire may grow at a slow or a fast rate, depending on
the type of combustion, the type of fuel, interaction with the surroundings,
and access to oxygen. The fire can be described in terms of the rate of
energy released and the production of combustion gases.
• A smoldering fire can produce hazardous amounts of toxic gases while the
energy release rate may be relatively low. The growth period of such a fire
may be very long, and it may die out before subsequent stages are reached.
• The growth stage can also occur very rapidly, especially with flaming
combustion, where the fuel is flammable enough to allow rapid flame
spread over its surface, where heat flux from the first burning fuel package is
sufficient to ignite adjacent fuel packages, and where sufficient oxygen and
fuel are available for rapid fire growth. Fires with sufficient oxygen available
for combustion are said to be fuel-controlled.

Flashover
• Flashover is the transition from the growth period to the fully developed
stage in fire development. The definition from ISO is “the rapid transition to
a state of total surface involvement in a fire of combustible material within
an enclosure.”
• Flashover is not a precise term: several variations in definition can be found
in the literature. The criteria given usually demand that the temperature in
the compartment has reached 500–600°C, or that the radiation to the floor
of the compartment is 15 to 20 kW/m, or that flames appear from the
enclosure openings.
• These occurrences may all be due to different mechanisms resulting from
the fuel properties, fuel orientation, fuel position, enclosure geometry, and
conditions in the upper layer. Flashover cannot be said to be a mechanism,
but rather a phenomenon associated with a thermal instability.

Fully developed fire
• At this stage the energy released in the enclosure is at its greatest and is very
often limited by the availability of oxygen. This is called ventilation controlled
burning (as opposed to fuel-controlled burning), since the oxygen needed for
the combustion is assumed to enter through the openings.
• In ventilation-controlled fires, unburnt gases can collect at the ceiling level,
and as these gases leave through the openings they burn, causing flames to
stick out through the openings.
• The average gas temperature in the enclosure during this stage is often very
high, in the range of 700 to 1200°C.

Decay
• As the fuel becomes consumed, the energy release rate diminishes and thus
the average gas temperature in the compartment declines.
• The fire may go from ventilation-controlled to fuel controlled in this period.

Fire development in terms of flow through openings
• A second way of dividing the fire into stages is to observe the mass flows in
and out through the enclosure openings while the fire progresses. The flows
depend on the pressure differences across the opening.
• The pressure for the outside atmosphere is represented by a straight line,
sloping because the weight of the column of air increases as one approach
the ground level. Assuming that the temperature of the air in the lower layer
of the compartment equals the temperature outside, one knows that the
pressure in the lower layer is given by a straight line with the same slope as
that for the outside. There is a kink in the pressure line inside when we move
into the upper layer; the hot air is lighter than the cold air.
• The pressure of the outside atmosphere is the same for all four cases and is
denoted by the symbol Po. The pressure inside the compartment is denoted
Pi.

Pressure profile across the opening as fire develops

• Stage A:
In the first stage of the fire the pressure inside is higher than the pressure
outside the compartment. This is due to the expansion of the hot gases,
which have a greater volume than the cold gases. If the opening is not at
ceiling level, the cold gases will be forced out through the opening due to
the hot gas expansion. As a result, the pressure difference across the
opening is positive and there will be no inflow through the opening, only
outflow of cold gases.
• Stage B:
This only lasts a few seconds and is often ignored. The smoke layer has just
reached the top of the opening and the hot gases have started to flow out.
The pressure inside is still higher than the pressure outside and both hot
and cold gases flow out through the opening. There is no mass flow into
the compartment.

• Stage C:
In this stage the hot gases flow out through the top of the opening and the
mass balance demands that cold gases of equal mass flow in through the
lower part of the opening. This stage can last for a considerable time, until
the room is filled entirely with smoke or until flashover occurs. Stages A, B,
and C are associated with the growth stage mentioned above and the
preflashover stage.
• Stage D:
This stage is often termed the “well-mixed” stage, where the compartment
is filled with smoke that is assumed to be well mixed, i.e., assumed to have
some single, average temperature. This stage is associated with the fully
developed fire mentioned above. In many cases flashover has occurred
between stages C and D.

Note
• In fire safety engineering design two distinctly different design situations
often occur.
1. One has to do with the pre-flashover fire, where the emphasis is on the
safety of humans. The design load in this case is characterized by an
energy release rate curve, where the growth phase of the fire is of most
importance.
2. A very different design situation arises when the objective is to ensure
structural stability and safety of firefighters. Here the post-flashover fire is
of greatest concern, and the design load is characterized by a
temperature–time curve where the fully developed fire stage is of greatest
concern.
• The fire development is therefore sometimes simply divided into the pre-
flashover stage and the post-flashover stage.

Note
• After ignition and during the initial fire growth stage, the fire is said to be
fuel-controlled, since, in the initial stages, there is sufficient oxygen available
for combustion and the growth of the fire entirely depends on the
characteristics of the fuel and its geometry.
• When the fire grows toward flashover it may become ventilation-controlled,
when there is not enough oxygen available to combust most of the
pyrolyzing fuel. The energy release rate of the fire is then determined by the
amount of oxygen that enters the enclosure openings, and the fire is
therefore termed ventilation-controlled. During the decay stage the fire will
eventually return to being fuel-controlled.
• The growth stage of the fire (and the pre-flashover fire) is therefore often
associated with the fuel-controlled fire, and the fully developed stage (and
the post-flashover fire) is often associated with the ventilation-controlled
fire.

• Carattere estensivo (diffusione nello spazio):
1. wildfire
2. urbanfire
• Carattere intensivo (andamento nel tempo).

CARATTERE INTENSIVO
II

1. Cosa e’ un incendio
2. Condizioni nelle quali si
sviluppa un incendio
3. Quanta energia puo’ essere
sviluppata in un incendio
4. Quale e’ la velocita’ con la
quale si sviluppa un incendio
1
2
3
4

Incendio: caratterizzazione (1)
• L'incendio è una reazione ossidativa (o combustione) non
controllata che si sviluppa nello spazio e nel tempo dando luogo,
dove si estende, a calore, fumo, gas e luce.
• La descrizione di un incendio consiste nella caratterizzazione
quantitativa del focolare come sorgente di energia termica e
prodotti della combustione, secondo:
1

• localizzazione del focolare;
• tipologia di focolare: covante o con fiamma;
• quantità, qualità e distribuzione spaziale del combustibile;
• fonti d'innesco;
• curva RHR (rate of heat released) o HRR (Heat Release Rate),
potenza termica prodotta dal focolare nel tempo RHR(t);
• prodotti della combustione considerati (es. CO e particolato).

Condizioni
• Per far sì che avvenga un incendio è necessario che siano presenti
tre elementi fondamentali:
1. combustibile: materiali infiammabili;
2. comburente: ruolo svolto usualmente dall'ossigeno;
3. temperatura (o calore): è necessaria la presenza di un'adeguata
temperatura affinché avvenga l'innesco.
• Combustibile e comburente devono essere presenti in proporzioni
adeguate definite dal campo di infiammabilità.
• Se non sono presenti uno o più dei tre elementi della combustione,
questa non può avvenire e – se l'incendio è già in atto – si
determina l'estinzione del fuoco.
2

Incendio non vincolato o vincolato (dall’ossigeno)
• Controllato dal combustibile - “NON VINCOLATO” (all'aperto, in
grandi ambienti o edifici con elevata superficie di ventilazione): la
quantità del combustibile determina l’entità dell’incendio; c’è
sovrabbondanza di ossigeno.
• Limitato dalla (superficie di) ventilazione - “VINCOLATO” (in edifici
con superficie di ventilazione ordinaria): è l’ossigeno che regola la
combustione; può esserci anche una grande quantità di
combustibile, ma non può bruciare adeguatamente perché non c’è
ossigeno sufficiente.

• L’incendio si può schematizzare come una sorgente di tipo
volumetrico, ossia un bruciatore che rilascia calore (HRR) e
quantità di particolato (soot) e di gas.
NB: Particolato carbonioso
E’ una polvere nera (essenzialmente carbonio incombusto amorfo,
più tracce di altri composti) che si può ottenere come sottoprodotto
della combustione incompleta di una qualsiasi sostanza organica
(anche fuliggine / nerofumo).

Unità di misura
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Energy
3
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Energy
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ISO 13387: Example of Design Fire

Evoluzione temporale potenza termica

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Power
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T-squared Fire (1)
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T-squared Fire (2)
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HRRf massimo tasso di rilascio termico prodotto da 1 mq di
incendio nel caso di combustione controllata dal combustibile.
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L’energia disponibile per essere rilasciata nell’incendio e’ l’area
sottesa dalla curva RHR e rappresenta il carico d’incendio [kJ] (in
ascissa il tempo [s] e in ordinata la potenza termica [KW] = [kJ s-
1]).
dinamica
30%
energia
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Fasi dell’incendio
• Prima fase (pre-flashover): funzione diretta della velocità di
combustione e del quantitativo di combustibile (energia)
disponibile; si ha una crescita di tipo quadratico, con pendenza
(velocità) in funzione del materiale e sue condizioni fisiche;
• Seconda fase: in ambiente chiuso si raggiunge, dopo un certo t,
una temperatura tale da provocare l’incendio di tutti i materiali; il
fattore determinante diventa la ventilazione e il materiale che può
bruciare dipende solo dalla ventilazione disponibile; si ha un
diagramma orizzontale, con RHRmax limitato dalla ventilazione;
• Terza fase: lineare, rappresenta il progressivo spegnimento.
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Sistemi di controllo
Sistemi di
spegnimento
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Sistemi di controllo dell’incendio
• Con sistemi di controllo dell'incendio automatici (es. sprinkler),
RHR(t) non raggiunge RHRmax, che poteva raggiungere in base a
combustibile e ambiente.
• RHR può essere assunto costante, pari a RHR(tx) rag-giunto
all’istante tX di entrata in funzione dell’impianto.
• Il valore permane per un tempo pari alla durata di alimentazione
prevista, entro cui si presume che l’incendio controllato venga
estinto con l’intervento manuale.
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Note
• Se nell'attività sono previsti sistemi automatici di estinzione
completa dell’incendio (es. sprinkler ESFR - early suppression fast
response, water mist, ecc.), il loro effetto deve essere valutato caso
per caso in relazione alla loro efficacia ed all'affidabilità di
funzionamento.
• A differenza dell’attivazione dei sistemi automatici, l’intervento
manuale effettuato dalle squadre antincendio non può essere
considerato in fase progettuale ai fini della modifica
dell'andamento della curva RHR(t).

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Come da Norme

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Rewind

Energy

Power

Analytic

Curve temperatura - tempo

Temperatura nel tempo
(curva naturale d’incendio)
180
5
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Summary of periods
of typical fire development
Incipient
period
Growth period Burning period Decay period
Fire
Behavior
Heating
of fuel
Fuel controlled burning Ventilation controlled
burning
Fuel controlled
burning
Human
behavior
Prevent
ignition
Extinguish by hand,
escape
Death
Detection Smoke
detectors
Smoke detectors, heat
detectors
External smoke and flame
Active
control
Prevent
ignition
Extinguish by sprinklers
or fire fighters; control
of smoke
Control by fire-fighters
Passive
control
- Select materials with
resistance to flame
spread
Provide fire resistance;
contain fire, prevent collapse
T
time
Buchanan, 2002 181
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F
L
A
S
H
O
V
E
R
passiva
▪ Create fire
compartments
▪ Prevent damage
in the elements
▪ Prevent loss of
functionality in
the building
attiva
▪ Detection measures
(smoke, heat, flame
detectors)
▪ Suppression
measures (sprinklers,
fire extinguisher,
standpipes, firemen)
▪ Smoke and heat
evacuation system
prevenzione protezione robustezza
▪ Limit ignition
sources
▪ Limit hazardous
human behavior
▪ Emergency
procedure and
evacuation
▪ Prevent the
propagation
of collapse,
once local
damages
occurred (e.g.
redundancy)
Strategie
182
time
T
21-Mar-23

Strategia antincendio: combinazione di misure di prevenzione,
protezione e gestionali per la riduzione del rischio di incendio.
active
protection
passive
protection
no
failures
doesn’t
trigger
Y
N
Y
N
spreads
extinguishes
damages
Y
N
robustness
no
collapse
collapse
Y
N
triggers
prevention
1 4
2 3
183
21-Mar-23

Curv nominali

CURVE NOMINALI
• CURVA STANDARD – CURVA ISO 834
• CURVA DEL FUOCO ESTERNO
tempo in minuti
temperatura dei gas caldi al tempo espressa in °C
• CURVA DEGLI IDROCARBURI
21-Mar-23

IMPOSTAZIONE DELLA SICUREZZA
III

Prevention
Prorection
Risk = Probability · Magnitudo
187
21-Mar-23

Risk
=
Probability
·Magnitudodo
discretization
in
log-log
plane
188
21-Mar-23

Risk
treatment
189
21-Mar-23

Option 1 – Risk avoidance, which usually
means not proceeding to
continue with the system;
this is not always a feasible
option, but may be the only
course of action if the
hazard or their probability of
occurrence or both are
particularly serious;
Risk
treatment
190
21-Mar-23

Option 2 – Risk reduction, either through
(a) reducing the probability
of occurrence of some
events, or (b) through
reduction in the severity of
the consequences, such as
downsizing the system, or
(c) putting in place control
measures;
Risk
treatment
191
21-Mar-23

Option 3 – Risk transfer, where insurance
or other financial
mechanisms can be put in
place to share or completely
transfer the financial risk to
other parties; this is not a
feasible option where the
primary consequences are
not financial;
Risk
treatment
192
21-Mar-23

Risk
treatment
Option 4 – Risk acceptance, even when it
exceeds the criteria, but
perhaps only for a limited
time until other measures
can be taken.
193
21-Mar-23

Option 1 – Risk avoidance, which usually means not proceeding to
continue with the system; this is not always a feasible option,
but may be the only course of action if the hazard or their
probability of occurrence or both are particularly serious;
Option 2 – Risk reduction, either through (a) reducing the probability of
occurrence of some events, or (b) through reduction in the
severity of the consequences, such as downsizing the system,
or (c) putting in place control measures;
Option 3 – Risk transfer, where insurance or other financial mechanisms
can be put in place to share or completely transfer the
financial risk to other parties; this is not a feasible option
where the primary consequences are not financial;
Option 4 – Risk acceptance, even when it exceeds the criteria, but
perhaps only for a limited time until other measures can be
taken.
194
21-Mar-23

Risk Analysis, Assessment, Management (IEC
1995)
Luur,
2002
195
21-Mar-23

Quantitative Risk Analysis
Luur,
2002
196
21-Mar-23

Risk-based decision making
Stewart
&
Melchers,
1997
197
21-Mar-23

RISK CONCERNS
DEFINE CONTEXT
(social, individual,
political, organizational,
technological)
RSK ANALYSIS
(for the system are defined organization,
scenarios, and consequences of
occurences)
RISK ASSESSMENT
(compare risks
against criteria)
RISK TREATMENT
option 1 - avoidance
option 2 - reduction
option 3 - transfer
option 4 - acceptance
MONITOR
AND
REVIEW
RISK
MANAGEMENT
RISK
ANALYSIS
RISK
ASSESSMENT
198
21-Mar-23

199
21-Mar-23

Scenarios
DEFINE SYSTEM
(the system is usually decomposed into
a number of smaller subsystems and/or
components)
HAZARD SCENARIO ANALYSIS
(what can go wrong?
how can it happen?
waht controls exist?)
ESTIMATE
CONSEQUENCES
(magnitude)
ESTIMATE
PROBABILITIES
(of occurrences)
DEFINE
RISK SCENARIOS
SENSITIVITY
ANALYSIS
RISK
ANALYSIS
FIRE
EVENT 200
21-Mar-23

Simulations
DEFINE SYSTEM
(the system is usually decomposed into
a number of smaller subsystems and/or
components)
HAZARD SCENARIO ANALYSIS
(what can go wrong?
how can it happen?
waht controls exist?)
ESTIMATE
CONSEQUENCES
(magnitude)
ESTIMATE
PROBABILITIES
(of occurrences)
DEFINE
RISK SCENARIOS
SENSITIVITY
ANALYSIS
RISK
ANALYSIS
NUMERICAL
MODELING
201
21-Mar-23

Prevention
Prorection
Risk = Probability · Magnitudo
202
21-Mar-23

Risk
=
Probability
·Magnitudodo
discretization
in
log-log
plane
203
21-Mar-23

21-Mar-23

Declinazione
al caso di incendio

Rischio, Rischio, Rischio (CPI)
• Rischio è la potenzialità che un'azione o un’ attivita’ scelta
(includendo la scelta di non agire) porti a una perdita o ad un
evento indesiderabile.
• Profilo di rischio e’ un indicatore speditivo della tipologia di
rischio di incendio associata all'esercizio ordinario di una qualsiasi
attivita’.
• Area a rischio specifico e’ una porzione dell'attivita’ caratterizzate
da rischio di incendio sostanzialmente differente rispetto a quello
tipico dell'attivita. L'individuazione delle aree a rischio specifico:
a. riportata nella regole tecniche verticali;
b. in assenza, e’ effettuata dal progettista secondo criteri
generali.
207
21-Mar-23

Profili di rischio (CPI)
208
21-Mar-23

Profilo di rischio Rvita
209
21-Mar-23

Caratteristiche occupanti
210
21-Mar-23

Velocita’ di sviluppo dell’incendio
211
21-Mar-23

Profilo di rischio Rvita
Incendio ---->
<----
occupanti
212
21-Mar-23

Profilo di rischio RBENI
213
21-Mar-23

Impostazione del progetto

Design Complexity
(Optimization)
Loosely – Tightly Couplings (Interactions)
Nonlinear–Linear
Behavior
215
21-Mar-23

DUE DILIGENCE
• Due diligence (also known as due care) is the effort made by
an ordinarily prudent or reasonable party to avoid harm to
another party. Failure to make this effort is considered
negligence.
• It is necessary to discover all risks and implications
regarding a decision to be made
• Due diligence is also a dynamic concept in that it is a
constantly evolving standard of care that is determined by
the requirements of law, industry standards as well as
professional and other codes of practice.
216
21-Mar-23

Design Process - ISO 13387
A. Design constraints and possibilities (blue),
B. Action definition and development
(red),
C. Passive system and active response (yellow),
D. Safety and performance
(purple).
217
21-Mar-23

SS0a
PRESCRIBED
DESIGN
PARAMETERS
SS0b
ESTIMATED
DESIGN
PARAMETERS
SS1
initiation and
development
of fire and
fire efluent
SS2
movement of
fire effluent
SS3
structural response
and fire spread
beyond enclosure
of origin
SS4
detection,
activitation and
suppression
SS5
life safety:
occupant behavior,
location and
condition
SS6
property
loss
SS7
business
interruption
SS8
contamination
of
environment
SS9
destruction
of
heritage
(0)
DESIGN
CONSTRAINTS
AND
POSSIBILITIES
(1+2)
ACTION
DEFINITION
AND
DEVELOPMENT
(3+4)
SYSTEM
PASSIVE
AND ACTIVE
RESPONSE
BUS
OF
INFORMATION
RESULTS
DESIGN
ACTION
RESPONSE
SAFETY
&
PERFORMANCE
218
21-Mar-23

Fire safety concepts tree (NFPA)
1
2
3
4
5
6
7
8
9
Buchanan,
2002
Strategie per
la gestione
dell'incendio
1
Prevenzione
2
Gestione
dell'evento
3
Gestione
dell'incendio
4
Gestione delle
persone e
dei beni
15
Difesa sul posto
16
Spostamento
17
Disposibilità
delle vie
di fuga
18
Far avvenire
il deflusso
19
Controllo
della quantità
di
combustibile
5
Soppressione
dell'incendio
10
Controllo
dell'incendio
attraverso il
progetto
13
Automatica
11
Manuale
12
Controllo dei
materiali
presenti
6
Controllo
del movimento
dell'incendio
7
Resistenza e
stabilità
strutturale
14
Contenimento
9
Ventilazione
8
219
21-Mar-23

Buchanan,
2002
1
2
3
4
5
6
7
8
9
Strategie per
la gestione
dell'incendio
1
Prevenzione
2
Gestione
dell'evento
3
Gestione
dell'incendio
4
Gestione delle
persone e
dei beni
15
Difesa sul posto
16
Spostamento
17
Disposibilità
delle vie
di fuga
18
Far avvenire
il deflusso
19
Controllo
della quantità
di
combustibile
5
Soppressione
dell'incendio
10
Controllo
dell'incendio
attraverso il
progetto
13
Automatica
11
Manuale
12
Controllo dei
materiali
presenti
6
Controllo
del movimento
dell'incendio
7
Resistenza e
stabilità
strutturale
14
Contenimento
9
Ventilazione
8
220
21-Mar-23

Line 2
• La gestione dell’incendio non è necessaria se si previene l’ignizione.
• Può essere solo ridotta la probabilità che avvenga l’ignizione.
• Gli incendi dolosi è difficile da prevedere dal progettista
221
21-Mar-23

Line 4
Exposed persons and property can be managed by moving them from the building or
by defending them in place; in order for people to move, the fire must be detected,
the people must be notified, and there must be a suitable safe path for movement.
222
21-Mar-23

Line 6
• There are three options for managing a fire; in the first case the fuel source can be
controlled, by limiting the amount of fuel or the geometry; the second options is to
suppress the fire; the third is to control the fire by construction.
• Control fire by construction it is necessary to both control the movement of the fire
and provide the structural stability.
223
21-Mar-23

Line 9 - The two strategies for controlling fire movement are:
a) fire venting: venting can be by an active system of mechanically operated vents, or a passive
system that relies on the melting of plastic skylights; in either case, the increased ventilation
may increase the local severity of the fire, but fire spread within the building and the overall
thermal impact on the structure will be reduced;
b) containment of a fire to prevent spread is the principal tool of passive fire protection;
preventing fire growing to a large size is ne of the most important components of a fire safety
strategy; radiant spread of the fire to neighboring buildings must also be prevented, by limiting
the size of openings in exterior walls;
Smoke containment can also controlled by venting or containment; pressurizations and smoke
barriers can also used.
224
21-Mar-23

• Line 4 – exposed persons and property can be managed by moving them from the
building or by defending them in place; in order for people to move, the fire must be
detected, the people must be notified, and there must be a suitable safe path for
movement.
• Line 6 – there are three options for managing a fire; in the first case the fuel source ca be
controlled, by limiting the amount of fuel or the geometry; the second options is to
suppress the fire; the third is to control the fire by construction.
• Control fire by construction it is necessary to both control the movement of the fire and
provide the structural stability.
Buchanan,
2002
225
21-Mar-23

• Line 9 - the two strategies for controlling fire movement are:
a) fire venting: venting can be by an active system of
mechanically operated vents, or a passive system that relies on
the meltig of plastic skylights; in either case, the increased
ventilation may increase the local severity of the fire, but fire
spread within the building and the overall thermal impact on
the structure will be reduced;
b) containment of a fire to prevent spread is the principal tool
of passive fire protection; preventing fire growing to a large
size is ne of the most important components of a fire safety
strategy; radiant spread of the fire to nighbouring buildings
must also be prevented, by limiting the size of openings in
exterior walls;
Smoke containment can also controlled by venting or
containment; pressurizations and smoke barriers can also
used.
Buchanan,
2002
226
21-Mar-23

PROGETTAZIONE PRESTAZIONALE
Fire Performance-based Desing

228
Processo di analisi
e processo di sintesi (1)
DATI
CALCOLO
RISULTATI
START
END
START
END
MODIFICA
K=K+1
K=0
DATI
K
CALCOLO
RISULTATI
K
TEST
SI’ NO
Pre-processing
Post-processing
21-Mar-23

229
Processo di analisi
e processo di sintesi (2)
START
END
MODIFICA
K=K+1
K=0
DATI
K
CALCOLO
RISULTATI
K
TEST
SI’ NO
ANALISI
SINTESI
21-Mar-23

PRESCRITTIVO / PRESTAZIONALE
APPROCCIO
PRESCRITTIVO
1) BASI DEL PROGETTO,
2) LIVELLI DI SCUREZZA,
3) PRESTAZIONI ATTESE
NON ESPLICITATI
1) REGOLE DI
CALCOLO E
2) COMPONENTI
MATERIALI
SPECIFICATI E
DETTAGLIATI
QUALITA' ED AFFIDABILITA'
STRUTTURALI
ASSICURATI IN MODO
INDIRETTO
GARANZIA DIRETTA DELLE PRESTAZIONI
E DELLA SICUREZZA STRUTURALI
INSIEME DI
STRUMENTI
LOGICI E
MATERIALI #3
INSIEME DI
STRUMENTI
LOGICI E
MATERIALI #1
INSIEME DI
STRUMENTI
LOGICI E
MATERIALI #2
OBIETTIVI
PRESTAZIONALI E
LIVELLI DI
SICUREZZA
ESPLICITATI
APPROCCIO
PRESTAZIONALE
NUMERICAL
MODELING
230
21-Mar-23

231
Prescrittivo
21-Mar-23

Prestazionale
232
21-Mar-23

START
APPLICAZIONE
DI
REGOLE
PRESTABILITE
E
TECNICHE
PREDEFINITE
END
START
END
DEFINIZIONE E DISANIMA
DEGLI OBIETTIVI
INDIVIDUAZIONE DELLE
SOLUZIONI ATTE A
RAGGIUNGERE GLI
OBIETTIVI
ATTIVITA' DI
MODELLAZIONE E MISURA
GIUDIZIO DELLE
PRESTAZIONI
RISULTANTI
No
Yes
21-Mar-23

234
MODELLI
NUMERICI
MODELLI
FISICI
RISPETTO DI
PRESCRIZIONI
livello
1
OBIETTIVI
livello
3
DEFINIZIONE
DELLA
SOLUZIONE
STRUTTURALE
livello
4
VERIFICA
DELLE
CAPACITA'
PRESTAZIONALI
LIMITI DELLA
PERFORMANCE i-esima
CRITERIO (QUANTITA')
CHE MISURA
LA PERFORMANCE i-esima
DEFINIZIONE DELLA
PERFORMANCE i-esima
livello
2
ESPLICITAZIONE DEGLI
OBIETTIVI ATTRAVERSO
L'INDIVIDUAZIONE DI n
PRESTAZIONI;
ordinatamente, per ciascuna di
esse, i =1,..n:
ESITO
NO
SI'
A
C
B
21-Mar-23

235
21-Mar-23

DECLINAZIONE SECONDO CPI

Strategie / Misure antincendio
• Strategia antincendio:
combinazione di misure
antincendio finalizzate
al raggiungimento degli
obiettivi di sicurezza
antincendio.
• Misura antincendio: categoria di
strumenti di prevenzione,
protezione e gestionali per ridurre
rischio incendio (S.1÷S.10).
237
21-Mar-23

238
Strategie
antincendio
21-Mar-23

Livello di prestazione:
reazione al fuoco
239
21-Mar-23

resistenza al fuoco
240
21-Mar-23

compartimentazione
241
21-Mar-23

esodo
242
21-Mar-23

Triangle
Shirtwaist
Fire,
1911
243
21-Mar-23

244
21-Mar-23

245
21-Mar-23

Soluzioni progettuali
• Soluzione conforme: soluzione di immediata
applicazione, che garantisce il raggiungimento del
livello di prestazione (Soluzione progettuale
prescrittiva che non richiede ulteriori valutazioni)
• Soluzione alternativa: il progettista è tenuto a
dimostrare il raggiungimento del livello di prestazione
(Soluzione progettuale prestazionale che richiede
ulteriori valutazioni).
• Soluzione in deroga: richiesta l'attivazione del
procedimento di deroga secondo la normativa
vigente.
246
21-Mar-23

Metodi ordinari di progettazione
della sicurezza antincendio
247
21-Mar-23

Metodi avanzati di progettazione
della sicurezza antincendi
248
21-Mar-23

Ingegneria della sicurezza antincendio
(metodo prestazionale,
Fire Safety Engineering - FSE)
Codice Prevenzione Incendi

Obiettivi e metodologia generale
per la progettazione della sicurezza antincendio

Classi di resistenza

S.2.1.

S.2.2.

S.2.3 Criteri di attribuzione dei livelli di prestazione (I)

S.2.3 Criteri di attribuzione dei livelli di prestazione (II)

S.2.3 Criteri di attribuzione dei livelli di prestazione (III)

S.2.3 Criteri di attribuzione dei livelli di prestazione (IV,V)

Soluzioni progettuali

Prescrittivo vs Prestazionale (1)
264

Prescrittivo vs Prestazionale (2)
265

conforme

Conforme

Alternative

Verifiche delle soluzioni progettuali

0
200
400
600
800
1000
1200
0 20 40 60 80 100 120
R60 945 ̊C
R30 842 ̊C
R15 739 ̊C R60 945 ̊C
R30 842 ̊C
R15 739 ̊C R90 1006 ̊C
Time [min]
R120 1049 ̊C
276
Standard (Conventional) Fire: ISO 834

Incendi convenzionali

Incendi naturali

Criteri di progetto

Carico di incendio specifico di progetto

21-Mar-23 287

Spessori conformi

21-Mar-23 298

NTC 2008
Norme Tecniche per le Costruzioni 2008

21-Mar-23 302
D.M. 14 gennaio 2008 (1)

D.M. 14 gennaio 2008 (2)

Indice 3.6.1. - INCENDIO
• 3.6.1.1 - Definizioni
• 3.6.1.2 - Richieste di prestazione
• 3.6.1.3 - Classi di resistenza al fuoco
• 3.6.1.4 - Criteri di progettazione
• 3.6.1.5 - Procedura di analisi della resistenza al fuoco
❑Incendio di progetto
❑Analisi dell’evoluzione della temperatura
❑Analisi del comportamento meccanico
❑Verifiche di sicurezza

3.6.1.1. Definizioni (1)

I – INCIPIENT PHASE
Heating of potential fuel is taking
place through combustion
processes.
II – GROWING PHASE
as other combustibles get involved
in the fire, a hotter upper layer of
smokes and combustion products is
formed , which becomes thicker as
the fire grows.
III – BURNING PHASE
the rate of heat release reaches the
max. and the burning rate remains
steady: usually most critical stage for
fire spread and structural damages.
IV – DECAY PHASE
Ignition Propagation Flashover Extinction
Peak
the burning rate decreases as all
combustible materials is consumed.
Temperatures of gases decrease,
until fire extinguishes.
306
21-Mar-23

Curve d’incendio nominali

3.6.1.5.1. Incendio di progetto

3.6.1.2. Richieste di prestazioni

3.6.1.3. Classi di resistenza al fuoco

3.6.1.4. Criteri di progettazione

• Ripristino di idonee condizioni al contorno.
• Riduzione opportuna delle sollecitazioni ordinarie a freddo (Ed) mediante un
coefficiente riduttivo ηfi,d
• Azioni indirette sull’elemento (quelle derivanti da deformazioni termiche impedite)
solo derivanti da gradienti termici lungo le sezioni strutturali trascurando le distorsioni
termiche assiali o quelle piane.
L’analisi di singole membrature deve risultare comunque conservativa
3 rotazioni
3 traslazioni
(K determinato a t = 0)
Analisi di singole membrature della struttura

(K determinato a t = 0
indipendente dal tempo)
3 rotazioni
3 traslazioni
• Ripristino di idonee condizioni al contorno.
• Riduzione opportuna delle sollecitazioni ordinarie a freddo (Ed) mediante un
coefficiente riduttivo ηfi,d
• All’interno della sottostruttura devono essere tenute in conto tutte le azioni
indirette, il decadimento delle proprietà meccaniche dei materiali, le effettive rigidezze
e il possibile meccanismo di collasso.
Non sono utilizzabili metodi tabellari. Metodi semplificati sono applicabili solo per
incendi nominali. Nel caso di incendi reali, invece, sono consentiti solo i metodi avanzati.
Analisi di parti della struttura

• Questo tipo di analisi strutturale è il più
completo.
• Può essere effettuato sia con regole
prescrittive che con un approccio
prestazionale.
• Sono utilizzabili solo metodi di calcolo
avanzati, che considerano le proprietà dei
materiali e la loro variazione con la
temperatura, le distorsioni termiche, il
verificarsi di meccanismi di collasso parziali,
la rigidezza delle membrature.
• Senza dubbio per la loro applicabilità
necessitano di grandi potenze di calcolo e di
una notevole specializzazione del progettista.
Analisi della struttura intera

3.6.1.5. Procedura di analisi di resistenza al fuoco
318
21-Mar-23

3.6.1.5.2. Analisi dell’evoluzione della temperatura
319
21-Mar-23

3.6.1.5.3. Analisi del comportamento meccanico
320
21-Mar-23

Mechanical Analysis
• The mechanical analysis shall be performed for the same duration
as used in the temperature analysis.
• Verification of fire resistance should be in:
–in the strength domain: Rfi,d,t ≥ Efi,requ,t
(resistance at time t ≥ load effects at time t);
–in the time domain: tfi,d ≥ tfi,requ
(design value of time fire resistance ≥ time required)
–In the temperature domain: Td ≤ Tcr
(design value of the material temperature ≤ critical material
temperature);
321
21-Mar-23

Verification of fire resistance (3D)
R = structural resistance
T = temperature
t = time
T=T(t)
R=R(t,T)=R(t,T(t))=R(t)

Verification of fire resistance (R-safe)
T = temperature
t = time
Rfi,d,t
Efi,requ,t

Verification of fire resistance (R-fail)
T = temperature
t = time
Efi,requ,t
Rfi,d,t
Failure !

Verification of fire resistance (t)
T = temperature
t = time
Efi,requ,t
Rfi,d,t
Failure !
tfi,d ≥ tfi,requ

Verification of fire resistance (T)
T = temperature
t = time
Efi,requ,t
Rfi,d,t
Failure !
Td ≤ Tcr

Esempio elementare

#4
328
21-Mar-23

#1
329
Scenario n
Scenario n°
°1
1 Scenario n
Scenario n°
°2
2
Scenario n
Scenario n°
°3
3 Scenario n
Scenario n°
°4
4
Scenario n
Scenario n°
°1
1 Scenario n
Scenario n°
°2
2
Scenario n
Scenario n°
°3
3 Scenario n
Scenario n°
°4
4
329
21-Mar-23

Initial deformed shape
Initial deformed shape: Scenario 1
Initial deformed shape
330
21-Mar-23

Levels of Structural Crisis
Usual
ULS
&
SLS
Verification
Format
Structural Robustness
Assessment
1st level:
Material
Point
2nd level:
Element
Section
3rd level:
Structural
Element
4th level:
Structural
System

INCENDIO

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INCENDIO