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Fire Modelling Joakim Sandstrom Lulea, 13 th -15 th of March 2014

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Page 1: Fire Modelling

Fire Modelling

Joakim SandstromLulea, 13th-15th of March 2014

Page 2: Fire Modelling

Introduction

• Smoke management depends strongly on geometry

Page 3: Fire Modelling

Introduction

• Smoke management depends strongly on geometry→ hard to standarise

Page 4: Fire Modelling

Introduction

• Smoke management depends strongly on geometry→ hard to standarise→ Prescriptive design often impossible

Page 5: Fire Modelling

Introduction

• Smoke management depends strongly on geometry→ hard to standarise→ Prescriptive design often impossible

• Engineering solutions needed!

Page 6: Fire Modelling

Introduction

• Smoke management depends strongly on geometry→ hard to standarise→ Prescriptive design often impossible

• Engineering solutions needed!

• This is where Fire Modelling comes into play

Page 7: Fire Modelling

Decisions to be made

• What kind of Fire Model?

Page 8: Fire Modelling

Decisions to be made

• What kind of Fire Model?• 0-D – Empirical Correlations (e.g. Heskestad’s

Plume Model)

Page 9: Fire Modelling

Decisions to be made

• What kind of Fire Model?• 0-D – Empirical Correlations (e.g. Heskestad’s

Plume Model)• 1-D – Zone Model

Page 10: Fire Modelling

Decisions to be made

• What kind of Fire Model?• 0-D – Empirical Correlations (e.g. Heskestad’s

Plume Model)• 1-D – Zone Model• 3-D – Computational Fluid Dynamics (CFD)

Page 11: Fire Modelling

Decisions to be made

• What kind of Fire Model?• 0-D – Empirical Correlations (e.g. Heskestad’s

Plume Model)• 1-D – Zone Model• 3-D – Computational Fluid Dynamics (CFD)

• What fire?

Page 12: Fire Modelling

Decisions to be made

• What kind of Fire Model?• 0-D – Empirical Correlations (e.g. Heskestad’s

Plume Model)• 1-D – Zone Model• 3-D – Computational Fluid Dynamics (CFD)

• What fire?→ Design fire based on use, geometry and fire load

Page 13: Fire Modelling

That being said....

Page 14: Fire Modelling

That being said....

The choice of Fire Model is not necessarily exclusive. Youmight need to use CFD and still use correlations.

Page 15: Fire Modelling

That being said....

The choice of Fire Model is not necessarily exclusive. Youmight need to use CFD and still use correlations.

Design fire need engineering judgement!→ There is no single solution..

Page 16: Fire Modelling

Design Fires

CIBSE Guide E

Page 17: Fire Modelling

Design Fires

• Most accepted growth model: t2-fire

Page 18: Fire Modelling

Design Fires

• Most accepted growth model: t2-fireQ = αt2

Page 19: Fire Modelling

Design Fires

• Most accepted growth model: t2-fireQ = αt2

• α depends on type of fuel

Page 20: Fire Modelling

Design Fires

• Most accepted growth model: t2-fireQ = αt2

• α depends on type of fuel→ Categorised according to use: office, storage,

dwellings etc.

Page 21: Fire Modelling

Design Fires

• Most accepted growth model: t2-fireQ = αt2

• α depends on type of fuel→ Categorised according to use: office, storage,

dwellings etc.

• Maximum Q depends on amount of fuel, or ventilationconfiguration

Page 22: Fire Modelling

Design Fires

• Most accepted growth model: t2-fireQ = αt2

• α depends on type of fuel→ Categorised according to use: office, storage,

dwellings etc.

• Maximum Q depends on amount of fuel, or ventilationconfiguration→ Engineering judgement..

Page 23: Fire Modelling

Design Fires

CIBSE Guide E

Karlsson – Enclosure Fire Dynamics

Page 24: Fire Modelling

Design Fires

CIBSE Guide E

Page 25: Fire Modelling

Design FiresThe maximum Heat Release Rate (Qmax) and fire duration haveto be estimated according to the following criteria:

Page 26: Fire Modelling

Design FiresThe maximum Heat Release Rate (Qmax) and fire duration haveto be estimated according to the following criteria:

• Ventilation condition (if flashover occurred)

Page 27: Fire Modelling

Design FiresThe maximum Heat Release Rate (Qmax) and fire duration haveto be estimated according to the following criteria:

• Ventilation condition (if flashover occurred)

• Total fuel load and Fuel density (if flashover hasn’toccurred)

Page 28: Fire Modelling

Design FiresThe maximum Heat Release Rate (Qmax) and fire duration haveto be estimated according to the following criteria:

• Ventilation condition (if flashover occurred)

• Total fuel load and Fuel density (if flashover hasn’toccurred)

• Engineering judgement

Page 29: Fire Modelling

Design FiresThe maximum Heat Release Rate (Qmax) and fire duration haveto be estimated according to the following criteria:

• Ventilation condition (if flashover occurred)

• Total fuel load and Fuel density (if flashover hasn’toccurred)

• Engineering judgement

Indications can be found in CIBSE Guide E, SFPE Handbookor NFPA.

Page 30: Fire Modelling

Some simple Calculations

2

Once we defined our Design Fire, Q(t), we can getestimations of important characteristics:

Page 31: Fire Modelling

Some simple Calculations

Once we defined our Design Fire, Q(t), we can getestimations of important characteristics:

• Air entrainment→ Volume of smoke

Page 32: Fire Modelling

Some simple Calculations

Once we defined our Design Fire, Q(t), we can getestimations of important characteristics:

• Air entrainment→ Volume of smoke

• Plume temperature

Page 33: Fire Modelling

Some simple Calculations

Once we defined our Design Fire, Q(t), we can getestimations of important characteristics:

• Air entrainment→ Volume of smoke

• Plume temperature

• Plume velocity

Page 34: Fire Modelling

Some simple Calculations

Once we defined our Design Fire, Q(t), we can getestimations of important characteristics:

• Air entrainment→ Volume of smoke

• Plume temperature

• Plume velocity

ment = E(

gρ2∞

T∞cp

)Q1/3c (z− z0)5/3 · [1 + GQ2/3

c(g1/2cpρ∞T∞)2/3(z−z0)5/3]

Page 35: Fire Modelling

Some simple Calculations

Once we defined our Design Fire, Q(t), we can getestimations of important characteristics:

• Air entrainment→ Volume of smoke

• Plume temperature

• Plume velocity

ment = E(

gρ2∞

T∞cp

)Q1/3c (z− z0)5/3 · [1 + GQ2/3

c(g1/2cpρ∞T∞)2/3(z−z0)5/3]

Tsmoke = T∞ + Qcmentcp

Page 36: Fire Modelling

Some simple Calculations

Once we defined our Design Fire, Q(t), we can getestimations of important characteristics:

• Air entrainment→ Volume of smoke

• Plume temperature

• Plume velocity

ment = E(

gρ2∞

T∞cp

)Q1/3c (z− z0)5/3 · [1 + GQ2/3

c(g1/2cpρ∞T∞)2/3(z−z0)5/3]

Tsmoke = T∞ + Qcmentcp

usmoke = 3.4 (g

ρ∞T∞cp

)1/3Q1/3c (z − z0)−1/3

Page 37: Fire Modelling

Why use Other Models?• For confined spaces, free plume correlations yield poor

results.

Page 38: Fire Modelling

Why use Other Models?• For confined spaces, free plume correlations yield poor

results.

• Heat transfer calculations from a fire to the structure.

Page 39: Fire Modelling

Why use Other Models?• For confined spaces, free plume correlations yield poor

results.

• Heat transfer calculations from a fire to the structure.

→ Requires more sophisticated models.

Page 40: Fire Modelling

Why use Other Models?• For confined spaces, free plume correlations yield poor

results.

• Heat transfer calculations from a fire to the structure.

→ Requires more sophisticated models.

→ If you need spatial resolution (e.g. location of exhaustoutlets, gas temperatures for heat transfer calculations),use field models (CFD).