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01-09-2008

Analysis of Hold Time Models for Total Flooding Clean Extinguishing Agents

Author: Todd M. Hetrick

Published in: Fire Technology | Issue 3/2008

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Abstract

This study documents the experimental results of a research program designed to evaluate the validity of the widely published hold time prediction models found in NFPA 2001, Annex C and ISO 14520-1, Annex E. The models discussed in these standards obtain a measure of the equivalent leakage area, which, when coupled with ‘worst case’ assumptions, can be used to determine the minimum hold time. Three hold time prediction theories are adopted from these standards for validation; a wide descending interface model as implemented in ISO 14520-1 and two sharp descending interface models from the 2004 and 2008 publications of NFPA 2001. The experimental program is comprised of 15 tests conducted in a 103 m3 test enclosure. Three commercially available clean agents are selected to span a wide range of agent vapor densities including FK-5-1-12, HFC-125, and IG-541. A series of holes were drilled through enclosure boundaries at upper and lower elevations which were opened or closed as a means of regulating the amount of leakage area for any given test. Vertical profiles of agent concentration and ambient pressure are used to evaluate the agent concentration distribution, rates of agent draining, and the effective lower leakage fraction. A non-dimensional hold time is used to compare experimental results involving differing agent types and leakage areas. Results show that empirical values of the hold time are up to 50% longer than the theoretical hold time predictions when evaluated as the time to reduce the agent concentration to half its initial value. When evaluated as a 15% drop in concentration the model validity is significantly reduced. Under this condition, empirical hold time values are up to 50% shorter than the predictions of the sharp descending interface models and up to 100% longer than the wide descending interface model.

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Footnotes
1
Bias pressures are typically created by HVAC systems; resulting in either a static or dynamic pressure differential between the enclosure’s interior and exterior. Observation and mathematical handling of bias pressures is integrated into the published editions of NFPA 2001 and ISO 14520-1. Bias pressures were eliminated from the test enclosure in this study; and thus, are not included in the theoretical derivations.
 
2
The flow exponent, n, has been set to 0.5 because the orifice flow equation will only represent the area of a real orifice when this condition is satisfied [1].
 
3
Experiments 2, 3, and 4 from the IG-541 test set involve relatively ‘tight’ leakage configurations. In these tests only, there was concern for the potential of over pressurization. Tests 2 & 3 left the ceiling vent open throughout the discharge and retention time. In Test 4 the ceiling vent was closed within a few seconds after the clean agent discharge ended. For all other tests this vent remained sealed closed.
 
4
Reference Table 2 for a listing of critical test configuration parameters.
 
5
The enclosure’s ambient pressure, temperature, and nozzle pressure were typically recorded for a 60-s duration during agent discharge. Ambient pressure transducers were used throughout the test duration only for the HFC-125 test series.
 
6
Tuure and Perco gas analyzers’ output circuitry was non-invasively monitored throughout operation. The ability to analyze the instruments’ electrical activity rather than a small, strip-chart printout greatly enhanced the author’s ability to ensure greater precision in these measurements.
 
7
Proper calibration of all gas sampling instrumentation was not available. A relative measurement technique was implemented in the scaling of agent concentration data. Recorded values were scaled into engineering units based on a Zero value (a 30 s average of sampled fresh air before discharge) and a Full-Scale value (an average of ≥90 s of data acquired after agent discharge had ended and readings had stabilized). Data traces exhibiting suspect behavior or failing to return to baseline values after the test duration are discarded.
 
Literature
1.
go back to reference Dewsbury J, Whiteley RA (2000) Review of fan integrity testing and hold time standards. Fire Technol 36(4), 249–265CrossRef Dewsbury J, Whiteley RA (2000) Review of fan integrity testing and hold time standards. Fire Technol 36(4), 249–265CrossRef
2.
go back to reference DiNenno PJ, Forssell EW (1989). Evaluation of the door fan pressurization leakage test method applied to Halon 1301 total flooding systems. J Fire Protect Eng, 1(4), 131–140CrossRef DiNenno PJ, Forssell EW (1989). Evaluation of the door fan pressurization leakage test method applied to Halon 1301 total flooding systems. J Fire Protect Eng, 1(4), 131–140CrossRef
3.
go back to reference Mowrer F (2006) Analysis of vapor density effects on hold times for total flooding clean extinguishing agents. In: Halon options technical working conference, 16th proceedings, Albuquerque, New Mexico, May 2006, pp 1–12 Mowrer F (2006) Analysis of vapor density effects on hold times for total flooding clean extinguishing agents. In: Halon options technical working conference, 16th proceedings, Albuquerque, New Mexico, May 2006, pp 1–12
4.
go back to reference O’Rourke ST (2005) Analysis of hold times for gaseous fire suppression agents in total flooding applications. Master thesis, University of Maryland, College Park MD O’Rourke ST (2005) Analysis of hold times for gaseous fire suppression agents in total flooding applications. Master thesis, University of Maryland, College Park MD
5.
go back to reference Dewsbury J, Whiteley RA (2000) Extensions to standard hold time calculations. Fire Technol 36(4), 267–278CrossRef Dewsbury J, Whiteley RA (2000) Extensions to standard hold time calculations. Fire Technol 36(4), 267–278CrossRef
6.
go back to reference Emmons HW (2002) Vent flows, chapter 2–3. In: The SFPE handbook of fire protection engineering, 3rd edn. NFPA, Quincy, MA Emmons HW (2002) Vent flows, chapter 2–3. In: The SFPE handbook of fire protection engineering, 3rd edn. NFPA, Quincy, MA
7.
go back to reference Saum D, Saum A, Messing M, Hupman J (1988) Pressurization air leakage testing for Halon 1301 enclosures. In: Substitutes and alternatives to chlorofluorocarbons and Halons. Washington, DC Saum D, Saum A, Messing M, Hupman J (1988) Pressurization air leakage testing for Halon 1301 enclosures. In: Substitutes and alternatives to chlorofluorocarbons and Halons. Washington, DC
8.
go back to reference ISO 14520-1 (2006) Gaseous fire extinguishing systems – physical properties and system design – part 1: general requirements. International Standards Organization, Geneva, Switzerland, Annex E ISO 14520-1 (2006) Gaseous fire extinguishing systems – physical properties and system design – part 1: general requirements. International Standards Organization, Geneva, Switzerland, Annex E
9.
go back to reference NFPA 2001 (2008) Standard on clean agent fire extinguishing systems. National Fire Protection Association, Quincy, MA, Annex C NFPA 2001 (2008) Standard on clean agent fire extinguishing systems. National Fire Protection Association, Quincy, MA, Annex C
10.
go back to reference NFPA 2001 (2004) Standard on clean agent fire extinguishing systems. National Fire Protection Association, Quincy, MA, Annex C NFPA 2001 (2004) Standard on clean agent fire extinguishing systems. National Fire Protection Association, Quincy, MA, Annex C
11.
go back to reference Genge C (2005) Preventing excessive enclosure pressures during clean agent discharges. In: Halon options technical working conference, 15th proceedings, Albuquerque, New Mexico, May, 2005, pp 1–16 Genge C (2005) Preventing excessive enclosure pressures during clean agent discharges. In: Halon options technical working conference, 15th proceedings, Albuquerque, New Mexico, May, 2005, pp 1–16
Metadata
Title
Analysis of Hold Time Models for Total Flooding Clean Extinguishing Agents
Author
Todd M. Hetrick
Publication date
01-09-2008
Publisher
Springer US
Published in
Fire Technology / Issue 3/2008
Print ISSN: 0015-2684
Electronic ISSN: 1572-8099
DOI
https://doi.org/10.1007/s10694-008-0047-7