GAPS Guidelines: Clean Agent Systems
GAPS Guidelines: Clean Agent Systems
INTRODUCTION
National Fire Protection Association (NFPA) documents describe a level of fire protection agreed on
by persons representing a variety of interests. The guidance in these documents does not reflect
unique conditions or special considerations, such as system performance under adverse conditions.
Nor does NFPA guidance reflect the increased systems reliability that Global Asset Protection
Services (GAPS) recommends for high valued properties.
This GAPS Guideline takes a position on the provisions of NFPA 2001 that GAPS believes require
clarification or changes. To understand the position, this GAPS Guideline must be read with a copy of
NFPA 2001. The provisions of the NFPA document are not repeated.
POSITION
General
This standard covers total flooding and local application clean agent systems. Equipment must be
listed by a nationally recognized testing laboratory such as Underwriters Laboratories Inc. (UL).
Current agents used in occupied areas are found in Table 1. GAP.13.6.0 states GAPS’ position on
clean agent halon replacements.
TABLE 1
Agents Recognized in NFPA 2001
Halocarbon Inert Gas
Agent Trade Name Manufacturer Agent Trade Name Manufacturer
HFC-23 (FE-13TM) Dupont IG-01 Argotec Minimax
HFC-227ea (FM-200®), (FE-227TM) Dupont IG-541 Inergen Ansul
HCFC Blend A (NAF S-III) NAFG IG-55 Argonite Ginge-Kerr
HCFC Blend B (Halotron®) American Pacific IG-100 NN100 Koatsu
Corporation
FK-5-1-12 (NovecTM 1230) 3MTM
Although many prospective halon substitutes have surfaced, no simple drop-in agent has been found.
Several of the current agents have come close, but have not been able to meet the safety
requirements for both occupied areas and the environment:
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GAP.13.6.1
• FIC-1311 is a very active cardiac sensitizer at extremely low concentrations. However, all of its
other qualities are outstanding, especially from an extinguishing and environmental standpoint.
• Care must be taken with using HCFC Blend A in occupied areas. The Class B cup burner test
results is 9.9%. When used in large-scale tests, extinguishment takes place well below cup
burner test results. Adding 20% to the cup burner values exceeds the NOAEL.
• HFC-125 has been marketed as a near drop-in replacement for Halon 1301. In most cases, the
piping can be reused, and only new storage containers and nozzles are needed.
Although used in total flooding applications for unoccupied areas, fine powdered aerosols are not
clean agents. Aerosol systems are covered by NFPA 2010.
System designers must be knowledgeable and competent. One way to demonstrate competency is
by certification. In the U.S. the National Institute for Certification of Engineering Technologies (NICET)
provides such a service for extinguishing system designers.
Use pre-engineered systems only in applications meeting listed room size and piping limitations.
Otherwise use engineered systems which are designed for the specific hazard being protected.
Submit proposed systems to GAPS’ Central Plan Review Office for review and acceptance.
Requirements for data to be reviewed are found in GAP.13.0.2. Make sure the equipment used is
listed, or the manufacturer is actively pursuing a listing. In the latter case, as part of the contract the
installer must agree to update the installed equipment to conform to the future listing requirements.
Although clean agents are effective on Class A surface fires, there are no current listing requirements
for deep seated or burrowing fires. Deep seated fires generally require higher concentrations and
longer soak periods.
Applications
Clean agent systems may be used in the following occupancies, alone or in combination with
sprinkler protection.
• Flight simulators;
• Archival storage of media and documents;
• Tape vaults;
• Enclosed electronic equipment with an extended discharge;
• Computer rooms without combustible accumulations;
• Cable rooms or tunnels;
• Aircraft under construction or undergoing maintenance;
• Motor homes under construction;
• Yacht cabins under construction;
• Dust collection systems;
• As an extinguishing agent in explosion suppression systems;
• Interior of wet benches in semiconductor fabrication, if decomposition products can be confined;
• Inerting systems to protect against potentially explosive gas vapors;
• Marine applications (machinery spaces, pump rooms, flammable liquids rooms, etc.).
Unsuitable Applications
In addition to those stated NFPA 2001, halocarbon-based clean agents are not suitable in the
following applications:
• Hot surfaces, such as ovens and furnaces operating above 700°F (371°C).
• High-energy electrical equipment such as transformers and switchgear equipment which cannot
be de-energized, where continuing arcing generates harmful quantities of decomposition products.
• Internal combustion engines.
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GAP.13.6.1
Agent Decomposition
The amount of decomposition products depends on fire size, intensity, speed of detection, speed of
system operation, length of discharge, and the presence of electrical arcing. If the concentration of
agent is insufficient to extinguish the fire or if the extinguishment time is prolonged, potentially harmful
amounts of corrosive and toxic by-products may be released. Formation of hydrofluoric acid (HF) in
some tests has been high enough to etch glass.
Hazards To Personnel
In occupied areas, use only extinguishing agents that ensure extinguishment at safe exposure levels.
GAPS does not specify design concentrations, but does require that the stipulations of this standard
be followed. If a system design concentration above the NOAEL is proposed by the system designer,
the purchaser of the protection system must understand the safety implications of exceeding the
NOAEL and be willing to proceed with the installation.
Halocarbon Exposure
Needless exposure to any extinguishing agent is discouraged. People should evacuate before the
system operates during a fire condition. If an accidental operation of the system occurs, evacuation of
all nonessential personnel should take place immediately. Those that remain in the room should use
breathing apparatus. Some halocarbon clean agent systems are designed near concentrations that
cause abnormal reactions in most people and can induce cardiac sensitization in some people.
Although halon suppresses fire by chemical chain breaking, most of the halocarbon clean agents rely
on thermodynamic cooling to extinguish combustion. Like halon, the halocarbon clean agent
extinguishing process releases corrosive decomposition products. Human exposure limits to HF are
found in the Annex of NFPA 2001. After discharge, prohibit smoking until the room has been purged
of halocarbon clean agents. Decomposition products of halocarbon clean agents produced by burning
smoking materials create strong acids that can be ingested.
Inert Gas Clean Agents
The inert gases extinguish fires by lowering the oxygen levels below that needed to support
combustion while leaving enough oxygen for minimal breathing. Under some conditions inert gas
clean agents can displace sufficient oxygen to become lethal. People with breathing problems would
be the first ones affected.
Inert gases do not create toxic decomposition products. Toxic combustion products are still produced
by the fire. When designing protection with inert gas agents, the higher the agent design
concentration the lower the enclosure’s residual oxygen content.
A discussion of O2 and CO2 levels is found in the Chapter on Toxicology in the SFPE Handbook of
Fire Protection Engineering.
Primary Agent Supply
Adjacent clean agent protected spaces may be considered as separate hazards if doors or dampers
protecting connecting openings are quickly and automatically closed when the first detector activates.
Design protection for each space as an independent system.
In adjacent areas where a fire may spread, design agent quantities for each area, but operate all
protection areas simultaneously.
Design systems to maintain the discharge concentration long enough to extinguish the fire and allow
fire fighting personnel time to arrive at the scene; ten minutes is usually long enough and is generally
an industry accepted hold time. Deep-seated hazards may require higher design concentrations and
longer soak periods.
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Shut down freestanding self-contained unit air conditioners preferably when the first detector
operates, unless the underfloor space is used as an air plenum for the computer equipment. In that
case, unit air conditioners may continue to run. In rooms with extremely high ceilings, fans may be
allowed to run to achieve a more homogeneous agent/air mixture. But in either case, the smoke
detection system will be less effective because detection is difficult when air is flowing at a high
velocity. Air sampling detection may be more appropriate here because of it sensitivity.
If dampers can be remotely reset, power the resetting devices by the primary source, the drain on the
emergency reserve battery power may be too great. Rapidly closing the dampers on large ducts can
collapse the ducts unless a pressure equalizing automatic damper is provided for the exhaust system.
In such a case, arrange dampers for slow shutdown.
In computer facilities, provide ventilation systems to exhaust the residual agent, its decomposition
2 3 2
products and combustion products. Design the exhaust system for 3 cfm/ft (0.15 m /min/m ) of floor
2 3 2
area in computer rooms, or 4 cfm/ft (0.20 m /min/m ) in underfloor areas and magnetic tape vaults.
Interlock the exhaust system so it cannot operate during the discharge and soak periods. Provide
makeup air from a clean source.
Design Concentration Requirements
Unlike Halon 1301, clean agents have a wide range of design concentrations based on the materials
that are expected to be involved in the fire.
When calculating protection volume, include all duct volumes that are cut off by dampers and are
within the protected space. Usually the protected enclosure is considered empty. However, deduct
large, permanent solid objects if the hazard is contained inside a relatively small enclosure. Failure to
make this deduction may result in an excessive concentration. Consider tape storage rooms as
empty.
Class A Extinguishment
Keep halocarbon clean agent discharge times of as short as possible to minimize formation of
decomposition products. Maintain design concentration for at least a 10 min soak period.
For Class A materials with deep seated characteristics, higher concentrations and longer soak
periods will be needed. Prove extinguishment of the specific fuel and arrangement in a large-scale
test for the specific agent and add 20% to the extinguishing concentration. Hold concentration for a
long enough period to ensure extinguishment. Generally, deep-seated fires require concentrations
that may exceed the limits for occupied areas. Therefore, provide adequate warning alarms to
evacuate personnel. Extinguishing agents, such as water, can handle deep-seated fires more
economically without excessive decomposition material generation.
Class B Extinguishment
The minimum agent concentration for extinguishment for Class B fires is determined by the cup
burner test. Previous cup burner data was inconsistent due to variation in cup burner apparatus and
test methods. A standard cup burner method with a defined test apparatus has been added to Annex
B of the standard for the 2008 edition. Values for minimum flame extinguishing concentrations based
on the previous editions of the standard have been retained, however it is anticipated that new values
will be developed based on the new cup burner standard and will be included in future versions of the
standard.
There is more HF generation with Class B fires due to the ease of agent by-products removing
loosely bonded H atoms from the fuel.
Maintain the concentration long enough to allow heated surfaces to cool to prevent reignition.
Inerting
Inerting concentrations are generally much higher than those needed for extinguishment. See the
table in the Annex for test results; add 10% for design concentration. Inerting prevents ignition from
occurring.
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Design Factors
Design systems as simply as possible. Agent mixing and distribution in systems involving complex
piping arrangements or selector valves can only be confirmed with a discharge test. Complex piping
systems have unbalanced piping layouts as well as many asymmetrical flow splits, layouts
discharging into multiple enclosures, or enclosures having obstructions to agent dispersal.
Design Factor For Enclosure Pressure
After determining the quantity of agent required for the specific hazard using the minimum design
concentration at the ambient enclosure temperature, adjust for ambient enclosure pressure. The
ambient enclosure pressure is affected by elevation and enclosure pressurization.
Local Application Systems
Currently there are no listed and approved local application systems, however several manufacturers
are developing local application systems. This chapter was added by the committee to provide basic
guidance for future systems. Local application systems should be installed in accordance with the
listing and the manufacturer’s design manual.
Container Test
Hydrostatic testing of halocarbon containers is not routinely conducted to avoid moisture in the
container. If the container shows signs of damage during routine examination, either replace the unit
or perform a hydrostatic test and dry the container thoroughly before refilling.
Although not addressed in the standard, conduct a hydrostatic test every 12 years on inert gas
containers that have not been refilled.
Pipe Pressure Test
Pressure testing cannot be done hydrostatically on halocarbon based agents because residual
moisture may be left in the system piping. Use extreme caution during pneumatic testing, because it
presents a severe safety hazard. Hydrostatic testing of inert gas piping is preferred.
Puff Test
In addition to performing GAPS’ visual check, the installing contractor should physically inspect all
system piping to ensure that all pipe joints and supports are tight enough to prevent leakage or
hazardous movement during discharge.
NFPA offers little guidance on how to conduct a “puff test.” This test may be performed by
discharging a sufficient flow of nitrogen through the system. The flow rate should be capable of
blowing off covers placed on the open nozzles. This test does not confirm the anticipated dynamic
discharge forces and only proves the piping is not completely obstructed. To confirm the dynamic
discharge forces, the test would have to simulate the system mass flow rates, which is essentially a
discharge test. When a discharge test is performed, this test can be omitted.
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