CARLETON Design Fires for Buildings

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CARLETON Design Fires for Buildings

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  • 1DESIGN FIRES FOR COMMERCIAL PREMISES

    Dr. Ehab Zalok

    Department of Civil and Environmental EngineeringCarleton University

    CIB-W014 Fire, Ottawa, 2008 2/24

    Background

    Codes are moving from traditionally prescriptive building codes towards performance-based codes. Canada: NBC05 and NFC05

    Increase in the use of engineering solutions and approaches in the design of fire safety in buildings.

    Performance-based designs are done by considering how the building and its fire protection systems perform in the event of a fire.

    Building performance is evaluated following a fire hazard analysis procedure.

  • 2CIB-W014 Fire, Ottawa, 2008 3/24

    Engineering ApproachPerformancebased Fire Protection

    Define project scope

    Identify goals

    Define stakeholder and design objectives

    Develop performance criteria

    Develop design fire scenarios

    Develop trial designs

    Evaluate trial designs

    Selected design meets performance criteria?

    Select the final design

    Prepare design documentation

    Performancebased design report

    Specification, drawings, and operational and maintenance manual

    Modify design or objectives

    Develop fire protection engineering design brief

    Yes

    No

    Engineering flowchart of Performancebased Fire Protection SFPE 2000.

    CIB-W014 Fire, Ottawa, 2008 4/24

    Performancebased Fire ProtectionChallenges - Opportunities

    Demands a better understanding of the fire hazards of materials and the dynamics of design fires.

    Quantitatively measure fundamental properties to evaluate the expected performance of a material, product, or assembly Data could be used with appropriate analytical or computational

    models

    Require accurate calculations methods to justify the performance to the authority having jurisdiction (AHJ)

    Data for the fire properties can be obtained from New or Modified standard test methods Index-based, pass-fail fire test methods (prescriptive-based) Performance (performance-based)

  • 3CIB-W014 Fire, Ottawa, 2008 5/24

    Fire Scenarios and Design Fires

    Fire hazard analysis requires the identification of: Fire scenarios that may occur in the building (Qualitative) Design fires that should be considered (Quantitative)

    Design fires Fire Resistance Tests

    CAN/ULC S101 & ASTM E119 & ISO 834-1

    t-squared fires 1

    Design fire curves Ignition growth flashover - fully developed - decay

    2)( ittHRR =

    CIB-W014 Fire, Ottawa, 2008 6/24

    Process for Developing Design Fires

    Identification of design fires Fire loads Type of combustibles Arrangement of combustibles Building characteristics

    Quantification of design fires Heat release rate (HRR) Production rate of toxic gases

    1. Fire load surveys of real buildings

    2. Literature3. Statistics

    1. Testing2. Computer modeling

  • 4CIB-W014 Fire, Ottawa, 2008 7/24

    (1) Design Fires ProjectObjectives

    Develop appropriate design fires representing fires in commercial buildings.

    1. Define fire loads and fuel packages representing the types of combustibles in commercial buildings.

    2. Produce experimental data showing the burning characteristics of the fuel packages.

    3. Develop input data files to be used in fire models (FDS) to represent the fuel packages in commercial premises.

    4. Use the input data files developed in Step 3 to model the burning characteristics in real-size stores.

    CIB-W014 Fire, Ottawa, 2008 8/24

    Research Methods

    Assessment of the Fire Load(Fire load survey+literature+Statistics)

    Design fuel Packages

    Conduct Phase I tests, ISO room Phase I modeling (FDS)

    Select fuel Packages for Phase II

    Conduct Phase II tests,Post-flashover

    Define appropriate design fires(HRR, hot layer temperature, and CO and CO2 production rates)

    Phase II modeling (FDS)

    Define appropriate input file in FDS to predict fire characteristics in real-size stores

    Predict burning characteristics

    Predict burning characteristics

    No

    Yes

    No

    Yes

  • 5CIB-W014 Fire, Ottawa, 2008 9/24

    Discrete FLD Values and PDF of the Lognormal Distribution

    2)ln(21

    21)(

    =x

    ex

    xf

    = population mean = standard deviation

    iciihmkQ =

    CIB-W014 Fire, Ottawa, 2008 10/24

    Mean (), 95th percentile (-)

    Combustibles Contribution to the FLD

    7 7

    47

    96

    18

    8.3

    60

    4141

    59

    0

    10

    20

    30

    40

    50

    60

    70

    80

    90

    100

    Textiles Plastics Wood/Paper Food Misc.

    % C

    ontr

    ibut

    ion

  • 6CIB-W014 Fire, Ottawa, 2008 11/24

    Fuel Packages Used in Design Fires for Medium/Large-Scale Tests

    Fast FoodShoe storeClothing storeClothing store

    BookstoreToy StoreStorage areaComputer store

    CIB-W014 Fire, Ottawa, 2008 12/24

    Fuel Packages Used in Design Fires for Medium/Large-Scale Tests

    Each fuel package (1.0 m2) represents the fire load density, method of display, and combustible products in the proportions determined in the survey

    % of fire load Test Title ID FLD

    (MJ/m2)Textiles Plastics Wood/

    paper Rubber/ leather

    Food products

    Computer store CMP-I 812 3.08 50.6 46.3 0.00 0.00 Storage area SA-I 2320 5.60 31.1 49.1 8.50 5.70 Clothing store CLS-I 661 55.0 6.00 37.0 2.00 0.00 Clothing store CLW-I 661 23.0 1.00 76.0 0.00 0.00 Clothing store CLC-I 661 86.0 2.00 12.0 0.00 0.00 Toy store TOY-I 1223 6.59 18.6 74.8 0.00 0.00 Shoe store SHO-I 4900 1.00 0.00 34.0 65.0 0.00 Bookstore BK-I 5305 0.40 0.00 99.6 0.00 0.00 Fast-food outlet FF-I 881 0.30 19.3 38.9 0.00 41.5

  • 7CIB-W014 Fire, Ottawa, 2008 13/24

    Experimental Set-up

    CIB-W014 Fire, Ottawa, 2008 14/24

    Heat Release per Unit Mass of Oxygen

    Constant net amount of heat is released per unit mass of oxygen consumed for complete combustion (Thornton 1917)

    Heat released has a value of 13.1 MJ/kg of O2 Organic solids/liquids and gases (Huggett 1980)

    Example: hexane (complete combustion):

    Oxygen Depletion Method (Janssens 1991)C6H14 + 9.5(O2 + 3.76N2) 6CO2 + 7H2O + 35.72N2

    oo&& AOOH

    a

    OeAO

    ACO

    CO MMmEEEQ

    22

    2

    2

    )1()1(12

    1)( +

    =

  • 8CIB-W014 Fire, Ottawa, 2008 15/24

    Heat Release Rate (HRR)

    0

    500

    1000

    1500

    2000

    2500

    3000

    0 600 1200 1800 2400 3000Time (s)

    Hea

    t Rel

    ease

    Rat

    e (K

    W)

    BK-IICLC-IICMP-IIFF-IISA-IISHO-IITOY-IISlow t-squaredMedium t-squaredFast t-squared

    Heat release data

    Test ID Pea

    k (k

    W)

    Tim

    e1 (M

    in)

    Gro

    wth

    rate

    CMP-II 2475 4:10 M-F SA-II 2385 2:45 F CLC-II 2660 3:30 M-F TOY-II 2570 4:15 F SHO-II 2555 4:00 M-F BK-II 2375 2:50 S-M FF-II 2700 6:15 S-M

    CIB-W014 Fire, Ottawa, 2008 16/24

    CO & CO2

    CO production rates (mg/kJ) CO2 production rates (mg/kJ)

    0

    2

    4

    6

    8

    10

    12

    14

    0 600 1200 1800 2400 3000Time (s)

    CO

    Pro

    duct

    ion

    (mg/

    kJ)

    BK-II CLC-II CMP-II FF-IISA-II SHO-II TOY-II

    0

    20

    40

    60

    80

    100

    120

    140

    0 600 1200 1800 2400 3000Time (s)

    CO

    2 Pro

    duct

    ion

    (mg/

    kJ)

    BK-II CLC-II CMP-II FF-IISA-II SHO-II TOY-II

    Growth / fuel-controlled flaming conditions (early decay), lowest of all phases.

    Ventilation-controlled, highest of all phases. (peak = 2-4 times the average)

    Smouldering > growth / fuel-controlled flaming conditions(combustion occurring at low temperature)

    Visibility and Tenability limits

  • 9CIB-W014 Fire, Ottawa, 2008 17/24

    Comparisons Between One and Two Packages (Experiments SA-I and SA-II)

    0

    500

    1000

    1500

    2000

    2500

    3000

    0 600 1200 1800 2400 3000Time (s)

    Hea

    t Rel

    ease

    Rat

    e (K

    W)

    SA-II

    SA-I

    0

    2

    4

    6

    8

    10

    12

    14

    0 600 1200 1800 2400 3000Time (s)

    CO

    Pro

    duct

    ion

    (mg/

    kJ)

    SA-II

    SA-I

    0

    20

    40

    60

    80

    100

    120

    140

    0 600 1200 1800 2400 3000Time (s)

    CO

    2 Pro

    duct

    ion

    (mg/

    kJ)

    SA-II

    SA-I

    HRR (KW)

    CO2 productionCO production

    CIB-W014 Fire, Ottawa, 2008 18/24

    Modeling Objectives

    Develop a simple input data file that generates the same fire characteristics as in Phases I and II, in details:

    1. Model the fuel packages(material properties and ideal stoichiometric coefficients)

    2. Simulate the burning characteristics of Phase I and II tests (HRR, hot layer temperature, CO and CO2 total production )

    3. Assess the simulation capability to predict the burning characteristic of real-size stores

    Modeling was conducted using the (CFD) model,Fire Dynamics Simulator (FDS) by (NIST)

  • 10

    CIB-W014 Fire, Ottawa, 2008 19/24

    Modelling & Simulation

    Challenges: Grid resolution Material density (kg/m3) Heat of vaporization (kJ/kg) Heat of combustion (kJ/kg) Ignition temperature (C)

    CIB-W014 Fire, Ottawa, 2008 20/24

    Sensitivity Analysis

    0

    200

    400

    600

    800

    1000

    1200

    1400

    1600

    1800

    2000

    0 600 1200 1800Time (s)

    Hea

    t Rel

    ease

    Rat

    e (K

    W)

    PMMA, original

    PMMA, 25% decrease in density

    0

    200

    400

    600

    800

    1000

    1200

    1400

    1600

    1800

    2000

    0 600 1200 1800Time (s)

    Hea

    t Rel

    ease

    Rat

    e (K

    W)

    PMMA, original

    PMMA, 25% decrease in HoV

    0

    200

    400

    600

    800

    1000

    1200

    1400

    1600

    1800

    2000

    0 600 1200 1800Time (s)

    Hea

    t Rel

    ease

    Rat

    e (K

    W)

    PMMA, original

    PMMA, 25% decrease in HC

    0

    200

    400

    600

    800

    1000

    1200

    1400

    1600

    1800

    2000

    0 600 1200 1800Time (s)

    Hea

    t Rel

    ease

    Rat

    e (K

    W)

    PMMA, original

    PMMA, 25% decrease inignition temperature

  • 11

    CIB-W014 Fire, Ottawa, 2008 21/24

    Modeling vs. Experimental Results

    0

    500

    1000

    1500

    2000

    2500

    3000

    0 600 1200 1800

    Time (s)

    Heat

    Rel

    ease

    Rat

    e (K

    W)

    FF-IIFDS-IIFF-IFDS-I

    Heat release rate (kW)

    0

    200

    400

    600

    800

    1000

    1200

    0 600 1200 1800Time (s)

    TC T

    empe

    ratu

    re @

    2.1

    -m h

    igh

    (o C) FF-II

    FDS-II

    Hot layer temperature (C)

    CIB-W014 Fire, Ottawa, 2008 22/24

    Modelling vs. Experimental Results(Total CO and CO2 produced)

    G a s d a t a

    T e s t T e s t I D

    Tota

    l CO

    (kg)

    Tota

    l CO

    2 (kg

    )

    C o m p u t e r s t o r e C M P - I I 6 . 0 9 1 0 9 . 3 0 F D S - I I 6 . 4 5 1 1 2 . 3 0 S t o r a g e a r e a S A -I I 5 . 7 4 2 3 0 . 3 0 F D S - I I 6 . 1 2 2 3 9 . 4 1 C lo t h in g s t o r e C L C - I I 2 . 1 1 1 0 1 . 8 0 F D S - I I 1 . 9 1 1 0 7 . 1 8 T o y s t o r e T O Y -I I 4 . 0 4 1 7 4 . 7 0 F D S - I I 4 . 4 5 1 8 0 . 7 9 S h o e s t o r e S H O - I I 8 . 0 5 3 1 1 . 2 0 F D S - I I 8 . 4 9 3 1 5 . 6 1 B o o k s t o r e B K -I I 6 . 0 1 4 0 9 . 4 0 F D S - I I 6 . 4 0 4 1 5 . 8 0

  • 12

    CIB-W014 Fire, Ottawa, 2008 23/24

    Fire in a 10 x 10 x 2.6-m Storewith two 6 x 2.6-m doors

    Modelling and simulation provide a cost-effective mean to examine how the system works

    CIB-W014 Fire, Ottawa, 2008 24/24

    Modeling 10 x 10-m Toy Store

    0

    200

    400

    600

    800

    1000

    1200

    1400

    0 600 1200 1800 2400 3000Time (s)

    Hot

    laye

    r tem

    pera

    ture

    ( oC

    )

    Hot layer temperature (C) Heat release rate (MW)

    0

    10

    20

    30

    40

    50

    60

    0 600 1200 1800 2400 3000Time (s)

    Hea

    t rel

    ease

    rate

    (MW

    )

    Theoretical peak 51.5 (MW)

    Temperature ranges from 700 to 1200C in an enclosure during the fully-developed fire (Karlsson and Quintiere,2000)

    Absolute peak HRR (MW) oo HA518.1=