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This presentation discusses the final decision on the storage temperature for extinguishing agents, based on flammability behavior and distribution challenges. It also addresses the uncertainties in gas analysis technology.
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International Aircraft Systems Fire Protection Working Group Phoenix, AZ, USA 26-27March 2003 Federal Aviation Administration WJ Hughes Technical Center, Fire Safety Section, AAR-440 Atlantic City Int'l Airport, NJ 08405 USA Engine Nacelle Halon Replacement,FAA, WJ Hughes Technical Center Point of Contact : Doug Ingerson Department of Transportation Federal Aviation Administration WJ Hughes Technical Center Fire Safety Branch, AAR-440 Bldg 205 Atlantic City Int'l Airport, NJ 08405 USA tel: 609-485-4945 fax: 609-485-7074 or 609-646-5229 email: Douglas.A.Ingerson@faa.gov web page: http://www.fire.tc.faa.gov/
International Aircraft Systems Fire Protection Working Group Phoenix, AZ, USA 26-27March 2003 Federal Aviation Administration WJ Hughes Technical Center, Fire Safety Section, AAR-440 Atlantic City Int'l Airport, NJ 08405 USA Major Topics for Review Overview of Work, October ’02 – March ’03 • Finalizing Environmental Test Parameters • Quantifying Halon Replacement • Evaluating Pool Fire Behavior • Finding Certification Distribution Near Term Plans • Complete Certification Distribution Work • Complete Pool Fire Evaluation • Evaluate Varied Agent Discharge Impact on Reignition Time Delay • Equivalence Testing
SLIDE# 3 International Aircraft Systems Fire Protection Working Group Phoenix, AZ, USA 26-27March 2003 Federal Aviation Administration WJ Hughes Technical Center, Fire Safety Section, AAR-440 Atlantic City Int'l Airport, NJ 08405 USA FINALIZING ENVIRONMENTAL TEST PARAMETERSExtinguishing agent storage temperature • Referring to the storage temperature of the extinguishing agent during fire testing • Agent storage temperature has been 100°F • Desire expressed for an additional storage temperature of –65°F • FINAL DECISION : Fire testing will be completed at an agent storage temperature of 100°F • Basis for decision • Flammability behavior • Based on a system of fuel, air, and extinguishing agent within a fixed volume having consistent ignition energy (similar to ASTM E-695) • Increasing pressure requires increasing agent concentration to remain nonflammable • Increasing temperature requires increasing agent concentration to remain nonflammable • Given this behavior for comparable combustion behavior • The peak concentration value for a higher temperature will provide adequate protection at lower temperature • The challenge is for the extinguishing agent to DISTRIBUTE and attain the peak value found at the higher temperature while being stored at a lower temperature • This can be demonstrated by non-fire, distribution test alone
SLIDE# 4 Graphic from : Illustrating increasing flammability envelope with increasing temperature 2 International Aircraft Systems Fire Protection Working Group Phoenix, AZ, USA 26-27March 2003 Federal Aviation Administration WJ Hughes Technical Center, Fire Safety Section, AAR-440 Atlantic City Int'l Airport, NJ 08405 USA FINALIZING ENVIRONMENTAL TEST PARAMETERSExtinguishing agent storage temperature
SLIDE# 5 Illustrating increasing flammability envelope with increasing temperature Graphic from : International Aircraft Systems Fire Protection Working Group Phoenix, AZ, USA 26-27March 2003 Federal Aviation Administration WJ Hughes Technical Center, Fire Safety Section, AAR-440 Atlantic City Int'l Airport, NJ 08405 USA FINALIZING ENVIRONMENTAL TEST PARAMETERSExtinguishing agent storage temperature
SLIDE# 6 International Aircraft Systems Fire Protection Working Group Phoenix, AZ, USA 26-27March 2003 Federal Aviation Administration WJ Hughes Technical Center, Fire Safety Section, AAR-440 Atlantic City Int'l Airport, NJ 08405 USA FINALIZING ENVIRONMENTAL TEST PARAMETERSExtinguishing agent storage temperature • Basis for decision (continued) : • Uncertainty due to gas analysis technology • NIST demonstrates possible difficulty with higher boiling point agent (CF3I) at low storage & environmental temperatures • Varying liquid/vapor fractions of extinguishing agent observed during discharge • Room temperature agent & fixture ventilation • Cold temperature agent/room temperature fixture ventilation • Cold temperature agent & fixture ventilation • NIST utilized relatively unobtrusive technology for gas analysis • No sample transport; sample analyzed in test environment during discharge events • Minimal impact on the agent distribution during its measurement • FAA Tech Center utilizing Statham-derivative technology • Gas sample is transported to sensor – sample is heated by transport path • Sensor assembly is a heated environment – sample is heated prior to measurement • Uncertainty at FAA Tech Center : • Gas analysis error - sample transport and measurement will heat and change liquid agent to vapor • The gas analysis error may not permit accurate description of the transport phenomena in the test fixture
SLIDE# 7 International Aircraft Systems Fire Protection Working Group Phoenix, AZ, USA 26-27March 2003 Federal Aviation Administration WJ Hughes Technical Center, Fire Safety Section, AAR-440 Atlantic City Int'l Airport, NJ 08405 USA FINALIZING ENVIRONMENTAL TEST PARAMETERSLower air mass flow rate • Lower air mass flow in the test fixture at the FAA Tech Center is too large • Lower air mass flow has been 1.0 lbm/s • Desire to see 0.2 – 0.4 lbm/s which match flows found in fielded nacelles • FINAL DECISION : Lower air mass flow rate will be 1.0 lbm/s • Basis for decision • Work at FAA Technical Center founded on testing completed at 1.0 lbm/s • Changing to lower mass flow will invalidate database for agent dispersion and fire testing • The test fixture at the FAA Technical center is capable of 0.7 lbm/s minimum • Decreasing ventilation rate typically decreases agent quantity required to meet certification • Lower mass flows move fire protection design towards non-ventilated compartments
SLIDE# 8 International Aircraft Systems Fire Protection Working Group Phoenix, AZ, USA 26-27March 2003 Federal Aviation Administration WJ Hughes Technical Center, Fire Safety Section, AAR-440 Atlantic City Int'l Airport, NJ 08405 USA Quantifying a Halon replacementInitial step – Basis/Process • Reignition time delay is the duration between the extinguishment of the fire and its subsequent reignition • Environmental constraints • Test fixture set up for one macroscopic test scenario • Macroscopic test scenario = one ventilation configuration + one fire scenario • Agent discharged within 1 second • Agent storage temperature of 100°F • A small collection of individually unique tests are performed • Intended to map the behavior of the replacement candidate • A quantity can be estimated as a possible equivalent to the performance of Halon 1301
SLIDE# 9 International Aircraft Systems Fire Protection Working Group Phoenix, AZ, USA 26-27March 2003 Federal Aviation Administration WJ Hughes Technical Center, Fire Safety Section, AAR-440 Atlantic City Int'l Airport, NJ 08405 USA Quantifying a Halon replacementInitial step - Illustration
SLIDE# 10 International Aircraft Systems Fire Protection Working Group Phoenix, AZ, USA 26-27March 2003 Federal Aviation Administration WJ Hughes Technical Center, Fire Safety Section, AAR-440 Atlantic City Int'l Airport, NJ 08405 USA Quantifying a Halon replacementFinal step - Basis • Process requires repeating 5 tests to determine if a quantity is halon equivalent • An unsuccessful quantity can be determined in as few as 2 tests • This process is based on the statistical behavior of past test results • Based on 7 test sequences; each sequence contained 5 replicate tests • Test sequences were varied conditions providing reignition delay results • Evaluated the trend of the reignition time delay over the 5 tests • Evaluation determined whether the sequence of 4 tests would continue to a fifth • This process was successful for 6 of the 7 test sequences
SLIDE# 11 International Aircraft Systems Fire Protection Working Group Phoenix, AZ, USA 26-27March 2003 Federal Aviation Administration WJ Hughes Technical Center, Fire Safety Section, AAR-440 Atlantic City Int'l Airport, NJ 08405 USA Quantifying a Halon replacementFinal step - Process • Process • The average reignition time delay and sample standard deviation for halon are known • Run tests 1 through 4 with the replacement candidate at repeated test condition • Beginning with test #2 • Calculate the running average of the reignition time delay for the replacement candidate • Determine if the running average falls within +/- 1 sample standard deviation (halon) of the halon average reignition time delay • If yes, continue; otherwise change mass and start again
SLIDE# 12 International Aircraft Systems Fire Protection Working Group Phoenix, AZ, USA 26-27March 2003 Federal Aviation Administration WJ Hughes Technical Center, Fire Safety Section, AAR-440 Atlantic City Int'l Airport, NJ 08405 USA Quantifying a Halon replacementFinal step - Process • Process (continued) • Run test #5 and perform the FINAL evaluation • The running average of the reignition time delay (RTD) for the replacement candidate must be equal to or greater than that of halon • The sample standard deviation for the replacement candidate must be less than or equal to that of halon
SLIDE# 13 International Aircraft Systems Fire Protection Working Group Phoenix, AZ, USA 26-27March 2003 Federal Aviation Administration WJ Hughes Technical Center, Fire Safety Section, AAR-440 Atlantic City Int'l Airport, NJ 08405 USA Evaluating Pool Fire BehaviorBackground • Purpose • Observe combustion behavior • Dependent upon a recirculation zone • Recirculation zone forms behind flame stabilizing baffle over the pool of fuel • Determine threat for use in equivalence procedure • Work description • Looked at impact on fire behavior • Varying upstream baffle height • Hot surface behaviors – tube arrays • 2 tube diameters • 2 tube lengths • 2 positions above fuel surface • 2 positions downstream from flame stabilizing baffle • 2 exposed fuel surface areas • Continually operating electrodes • Characterize fire growth • Performed tests without discharging agent
SLIDE# 14 International Aircraft Systems Fire Protection Working Group Phoenix, AZ, USA 26-27March 2003 Federal Aviation Administration WJ Hughes Technical Center, Fire Safety Section, AAR-440 Atlantic City Int'l Airport, NJ 08405 USA Evaluating Pool Fire BehaviorUpstream baffle height • Reviewed literature for experience • Work by Hirst, Farendon, et al. • Indicated 1” baffle height worst case; demonstrated by : • Blow-off velocity • Agent concentration • Ran tests to observe fire behavior related to baffle height • Used baffle heights of 0.50”, 1.50”, & 2” • Exposed fuel surface area of 10.8”x10.8” • Fuel depth of 0.50” • Tube array used to monitor heating ability of fire • 4 straight tubes in a rhombus stack, 24” long x 0.50”OD • Supported 2.25” above fuel surface and 4.25” downstream from baffle • Observations; as baffle height increased : • Tube array temperature increased • Temperatures 16” & 30” downstream decreased • Hottest tube array temperature NOT comparable to profiles observed in hot surface ignition in the spray fire scenario
SLIDE# 15 CORE Exposed fuel surface Flame stabilizing baffle/rib AIRFLOW STA 527 STA 518 thermocouples UP STA 502 FWD This assembly not present during testing International Aircraft Systems Fire Protection Working Group Phoenix, AZ, USA 26-27March 2003 Federal Aviation Administration WJ Hughes Technical Center, Fire Safety Section, AAR-440 Atlantic City Int'l Airport, NJ 08405 USA Evaluating Pool Fire BehaviorUpstream baffle height - Illustration
SLIDE# 16 International Aircraft Systems Fire Protection Working Group Phoenix, AZ, USA 26-27March 2003 Federal Aviation Administration WJ Hughes Technical Center, Fire Safety Section, AAR-440 Atlantic City Int'l Airport, NJ 08405 USA Evaluating Pool Fire BehaviorHot surface/tube array - Descriptions • Purpose • Further observation of the fire behavior • Determine the surface area of the pool for the final threat in the equivalence process • Determine worst case tube array for evaluation against agent discharge • Altered tube array characteristics • 0.25” & 0.50” diameters • 5” & 10” tube lengths • Tube array supported 0.25” and 1” above fuel surface • Located 2”, 4”, 8”, 12”, & 16” downstream from flame stabilizing baffle • 10.8”x10.8” & 10.8”x20.5” exposed fuel surface areas • Tube array consisted of 3 tubes stacked in an inverted triangular wedge • Thermocouple imbedded in tube array at the middle of the tube length • Fuel depth of 0.50” • Ran multiple tests evaluating the various conditions described
Tube Array End View SLIDE# 17 flame stabilizing rib UP + + + 1/4”OD x 10” tubes AIRFLOW thermocouple 10.8” x 10.8” fuel surface area International Aircraft Systems Fire Protection Working Group Phoenix, AZ, USA 26-27March 2003 Federal Aviation Administration WJ Hughes Technical Center, Fire Safety Section, AAR-440 Atlantic City Int'l Airport, NJ 08405 USA Evaluating Pool Fire BehaviorHot surface/tube array - Illustration AIRFLOW
SLIDE# 18 International Aircraft Systems Fire Protection Working Group Phoenix, AZ, USA 26-27March 2003 Federal Aviation Administration WJ Hughes Technical Center, Fire Safety Section, AAR-440 Atlantic City Int'l Airport, NJ 08405 USA Evaluating Pool Fire BehaviorHot surface/tube array – Observations • Tube array temperatures attaining 1250 – 1325°F • Temperatures consistently hotter when : • Tube diameter was 0.25” • Tube array was downstream 4” or less from baffle • Tube array was supported 1” above fuel surface • Larger fuel surface area produced greatest thermal output • Larger fuel surface had no apparent impact on heating the tube array
SLIDE# 19 International Aircraft Systems Fire Protection Working Group Phoenix, AZ, USA 26-27March 2003 Evaluating Pool Fire BehaviorHot surface/tube array – Tube array temperatures
SLIDE# 20 International Aircraft Systems Fire Protection Working Group Phoenix, AZ, USA 26-27March 2003 Federal Aviation Administration WJ Hughes Technical Center, Fire Safety Section, AAR-440 Atlantic City Int'l Airport, NJ 08405 USA Evaluating Pool Fire BehaviorContinually operating electrodes - Descriptions • Purpose • Further observation of the fire behavior • Determine worst case electrode configuration for evaluation against agent discharge • Conditions for analysis • Electrode gap of 0.13” • Position gap 1.25”, 0.25”, 0.016”, & 0” above fuel surface • Electrode gap placed 0.5”, 2”, 5”, 10”, & 17” downstream from flame stabilizing baffle • Electrode gap placed on fore/aft center line of the pool • 10.8”x20.5” exposed fuel surface area • Fuel depth of 0.50” • No tube array • Marked fuel pan to determine flame propagation behavior • Ran multiple tests evaluating the various conditions described
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SLIDE# 23 International Aircraft Systems Fire Protection Working Group Phoenix, AZ, USA 26-27March 2003 Federal Aviation Administration WJ Hughes Technical Center, Fire Safety Section, AAR-440 Atlantic City Int'l Airport, NJ 08405 USA Evaluating Pool Fire BehaviorContinually operating electrodes - Observations • Pool did not ignite unless electrode gap was in contact with fuel surface • Flames propagated across the surface of the pool faster opposing the bulk air flow in the test section • Shortest duration to full pan involvement occurred with mobile electrode gap located 17” downstream from the flame stabilizing baffle
SLIDE# 24 International Aircraft Systems Fire Protection Working Group Phoenix, AZ, USA 26-27March 2003 Federal Aviation Administration WJ Hughes Technical Center, Fire Safety Section, AAR-440 Atlantic City Int'l Airport, NJ 08405 USA Evaluating Pool Fire BehaviorContinually operating electrodes - Observations
SLIDE# 25 International Aircraft Systems Fire Protection Working Group Phoenix, AZ, USA 26-27March 2003 Federal Aviation Administration WJ Hughes Technical Center, Fire Safety Section, AAR-440 Atlantic City Int'l Airport, NJ 08405 USA Evaluating Pool Fire BehaviorContinually operating electrodes - Observations
SLIDE# 26 International Aircraft Systems Fire Protection Working Group Phoenix, AZ, USA 26-27March 2003 Federal Aviation Administration WJ Hughes Technical Center, Fire Safety Section, AAR-440 Atlantic City Int'l Airport, NJ 08405 USA Evaluating Pool Fire BehaviorConclusions • Varied baffle heights • No reason suggested by data that 1” tall baffle is not worst case • Further evaluation required • Tube array • Tubes apparently not hot enough for hot surface ignition based on spray fire results • Worst case tube configuration • Exposed fuel surface of 10.8” x 20.5” length • Three 0.25”OD x 10” long tubes • Tube array located 4” downstream from baffle and supported 1” above fuel • Electrodes • Fastest pan fire developed when electrodes were positioned at the aft end of the pool • Recirculation zone is clearly present • Worst case electrode configuration • Location of 17” downstream from baffle • Electrode gap touched fuel at surface
SLIDE# 27 International Aircraft Systems Fire Protection Working Group Phoenix, AZ, USA 26-27March 2003 Federal Aviation Administration WJ Hughes Technical Center, Fire Safety Section, AAR-440 Atlantic City Int'l Airport, NJ 08405 USA Evaluating Pool Fire BehaviorConclusions (continued) • General comments • Tube array apparently not hot enough for hot surface ignition in any configuration attempted • The hottest tube array was located above the fuel in a region where the electrodes could NOT ignite the pool • Final determination to be made with worst cases tested individually & combined against the discharge of a fire extinguishing agent
SLIDE# 28 International Aircraft Systems Fire Protection Working Group Phoenix, AZ, USA 26-27March 2003 Federal Aviation Administration WJ Hughes Technical Center, Fire Safety Section, AAR-440 Atlantic City Int'l Airport, NJ 08405 USA Agent Distribution SearchBackground • Former Halon quantities producing certification at a storage temperature of –65°F • 5.2 lbf Halon 1301 @ ventilation of 2.2 lbm/s & 100°F • 3.2 lbf Halon 1301 @ ventilation of 1.0 lbm/s & 280°F • These quantities produced excessive concentration profiles since fire testing was occurring at at an agent storage temperature of 100°F • Work occurring to find agent quantities that will produce certification at a storage temperature of 100°F • 5.2 lbf Halon 1301 will be in the 3.5 – 4.0 lbf range • No estimate for reduction from 3.2 lbf Halon 1301
SLIDE# 29 International Aircraft Systems Fire Protection Working Group Phoenix, AZ, USA 26-27March 2003 Federal Aviation Administration WJ Hughes Technical Center, Fire Safety Section, AAR-440 Atlantic City Int'l Airport, NJ 08405 USA 3.90 lbf Halon 1301 @ ventilation of 2.2 lbm/s & 100°F Agent Distribution SearchPreliminary results
SLIDE# 30 International Aircraft Systems Fire Protection Working Group Phoenix, AZ, USA 26-27March 2003 Federal Aviation Administration WJ Hughes Technical Center, Fire Safety Section, AAR-440 Atlantic City Int'l Airport, NJ 08405 USA Near Term Plans • Complete certification distribution work • Finalize work at ventilation rate of 2.2 lbm/s @ 100°F • Accomplish work for the condition of 1.0 lbm/s @ 280°F • Complete pool fire evaluation • Run new quantities of halon against the pool fire • Determine which worst case to use in the equivalence procedure • Evaluate the impact of varied agent storage pressure on reignition time delay • Store the same amount of agent in the same volume at the same temperature • Alter storage pressure • Observe impact on the reignition time delay • Incorporate experience into the equivalence procedure • Equivalence testing