according to the present invention , a pre - packed solid gas generator is used for generating a gas mixture that is suitable for suppressing a fire from a solid non - azide chemical . preferably , the solid chemical ( not shown ) used in the solid gas generator ( s ) may be similar to those used as gas generators for automobile air bags . the solid chemical does not contain azides . azide compositions can be regarded as harmful to human health , and furthermore , often generate less gas by weight relative to non - azide compositions . newer generation automotive air bags for cars utilize such non - azide systems and any of these may be used n solid gas generators . in operation , solid gas generators produce an inert or near inert gas such as nitrogen , which reduces the concentration of oxygen in a room below the level that will sustain combustion . however , the oxygen concentration is maintained at a sufficient level to meet the requirements of the national fire prevention association &# 39 ; s 2001 standard for clean agent halon 1301 alternatives in normally occupied areas . the person having ordinary skill in this art knows that the national fire protection association &# 39 ; s 2001 standard ( published by the nepa entitled nfpa 2001 standard on clean agent fire extinguishing systems (“ nfpa 2001 ”), cited in an information disclosure statement filed concurrently herewith ) states in section 1 - 1 of the document : 1 - 1 scope . this standard contains minimum requirements for total flooding and local application clean agent fire extinguishing systems . it does not cover fire extinguishing systems that use carbon dioxide or water as the primary extinguishing media , which are addressed by other nfpa documents . ( emphasis added ) as shown in fig1 a and 1b . a gas generator fire suppression tower 1 is provided containing a pre - packed non - azide solid propellant canister 3 and a discharge diffuser 5 for discharging generated gases . the tower 1 is secured in position by floor mounting bolts 7 passing through a mounting flange 10 , or any other suitable means . the diffuser 5 is likewise secured to the tower 1 using flange bolts with nuts 6 . as is evident from fig1 a and 1b , a longitudinal axis ( not shown ) extends upward from the bottom of the flange 10 , through the tower 1 , the canister 3 , a propeller retainer 12 , the filters / screens 13 , and out the top of the diffuser 5 . a pyrotechnic device 9 ( i . e . a squib ) is attached to the pre - packed canister 3 by way of a connector 11 , and to a fire detection and release control panel discussed in greater detail with reference to fig2 a and 3 . the squib is used to initiate the inert gas generation in response to electrical activation . 1 - 5 . 1 . 1 the fire extinguishing agents addressed in this standard shall be electrically nonconducting and leave no residue upon evaporation . furthermore , the definition of clean agent is specified in section 1 - 3 . 8 of the nfpa 2001 document as follows : 1 - 3 . 8 clean agent . electrically nonconducting , volatile , or gaseous fire extinguishant that does not leave a residue upon evaporation . the word agent as used in this document means clean agent unless otherwise indicated . a propellant retainer 12 is provided along with various optional filters and / or screens 13 , as discussed in greater detail below . turning to fig2 a in combination with fig3 , the discharge diffuser 5 is shown having a perforated cap 15 . a raceway ceiling mounting foot 17 is provided for securing a conduit / wiring raceway 19 ( e . g . steel pipe ) between the fire detection and release panel 21 ( fig3 ) and a conduit connection 23 on a bracket 25 . the conduit continues downwardly to the squib 9 , as shown at 27 . fig2 b - 2d show alternative embodiments of discharge diffusers 5 , for different installations of the tower 1 , which may serve either as replacements for the perforated cap diffuser or be placed thereover . more particularly , fig2 b depicts a 180 ° directional different cap 5 a useful for installations wherein the tower is disposed along a wall . fig2 c depicts a 360 ° directional diffuser cap 5 b useful for installations wherein the tower is centrally disposed . fig2 d depicts a 90 ° directional diffuser cap 5 c useful for installations wherein the tower is disposed in a corner . with reference to fig3 , a system is shown according to the present invention for suppressing fires in an enclosed space using a plurality of towers 1 as set forth in fig1 and 2 . in operation , a sensor 31 , upon detecting a fire , issues a signal to the control panel 21 which , in response , activates an alarm signaling device 33 ( e . g . audible and / or visual alarm ). alternatively , an alarm may be initiated by activating a manual pull station 35 . in response , the control panel 21 initiates a solid gas generator by igniting the pyrotechnic device 9 , which in turn ignites the chemicals in the pre - packed canister 3 that produce the fire suppressing gas . the fire suppressing gas mixture preferably comprises nitrogen gas and may contain water vapor and / or carbon dioxide . however , as discussed above , the chemicals used in the solid gas generator do not contain azides . as indicated above , the fire suppressing gas mixture may contain carbon dioxide and water vapor , which are optionally filtered using filters 13 ( fig1 ), resulting in the production of a filtered fire suppressing gas mixture . more particularly , the fire suppressing gas mixture may be filtered so that the gas introduced into the room ( fig3 ) contains from about zero to about five wt % carbon dioxide and preferably , from about zero to about three wt % carbon dioxide . more preferably , substantially all of the carbon dioxide in the mixture is filtered out of the mixture . the fire suppression gas mixture may also be filtered so that the gas introduced into the room will not form any substantial amount of liquid water when introduced into the environment of the fire . preferably , the concentration of water vapor in the environment of the fire is maintained so that the water vapor is maintained above its dew point . moreover , screens may be used to reduce the temperature of the fire suppressing gas generated as a result of igniting the pre - packed canister 3 . although the filters and screen ( s ) 13 are shown as being separate from the pre - packed canister 3 , it is contemplated that at least the screen ( s ) may be incorporated as part of the canister structure . since there is no requirement to use compressed gas cylinders , discharge piping and discharge nozzles for the supply or transport of an extinguishing gas mixture , the system of fig3 enjoys several advantages over the known prior art . firstly , the use of only non - axide solid gas generators allows large amounts of gases to be generated with relatively low storage requirements . this reduces the cost of the system , making it more attractive to retrofit existing halon 1301 systems with environmentally acceptable alternatives ( i . e . inert or near - inert gasses are characterized as being zero ozone depleting and have zero or near - zero global warming potential ). secondly , the system benefits from simplified installation and control since all of the solid gas generators need not be provided at one central location . instead , one or more solid gas generators or towers 1 are preferably positioned at the location where the fire will have to be suppressed . in this way , the generation of fire suppressing gases within the hazard area , substantially simplifies the delivery of the gases without the need of a piping system extending throughout a building or perhaps through one or two walls . thirdly , the provision of independently positioned towers 1 results in the gas being generated and delivered to the hazard area almost instantaneously as it is released . this increases the response time of the fire suppressing system and it &# 39 ; s ability to inert the hazard area and suppress the fire in a normally occupied area . each solid gas generator 1 is preferably designed to generate a quantity of gas needed to extinguish a fire in room , should the need aris . the filtered fire suppressing gas mixture is delivered into the room ( fig3 ) containing a fire . the volume of filtered fire suppressing gas to be delivered into the room depends on the size of the room . preferably , enough of the filtered fire suppressing gas mixture is delivered into the room to suppress any fire in the room , yet still permit the room to be habitable by human life for a predetermined time . more preferably , a volume of filtered fire suppressing gas mixture is delivered into the room that permits the room to be habitable by human life for approximately one to five minutes , and more preferably from three to five minutes , as per the requirements of the national fire prevention association &# 39 ; s 2001 standard for halon 1301 clean agent alternatives in normally occupied areas . referring now to the alternative embodiment of fig4 , an illustration and part al cross section is provided of a single gas generator unit mounted in a corner of a room to be protected . in this embodiment , the fire protection unit 110 is a floor mounted unit , in a room 120 to be protected from fire . the unit 110 is located in a space in the room that does not inhibit normal use of the room by occupants , or desired positioning of other equipment . an integral smoke or heat detector 130 is mounted on the unit 110 in this embodiment , although it can also be wired to normal ceiling - mounted smoke detectors . upon detection of a fire or smoke by the detector 130 , it sends an electrical signal to the propellant squib 140 that initiates the burning of the gas generator propellant 150 , which generates the inert gas 160 in sufficient quantities to extinguish fires in an occupied compartment , discharged through the orifices or diffuser 170 , in the exterior of the unit 110 . such a system , mounted directly into the room to be protected , eliminates the expense of distribution plumbing from a remote storage site , and the expense of its installation . in a variation of this alternative embodiment , the unit 110 can be suspended to hang from the ceiling , or mount directly on the wall , including the use of a wall bracket similar to those used to position televisions in hospital rooms . fig5 is an illustration of single gas generator room unit , comprised of multiple gas generator cartridges . in this variation to the system disclosed in fig4 , the unit 210 houses multiple individual gas generator units 220 , each sized of a particular capacity to provide a sufficient quantity of inert gas for a given volume of occupied space . an internal rack 230 is ; a means of selectively installing a variable number of units 220 , each with their own squib 240 and wired to the detector 250 , to provide a precise quantity of inert gas necessary to protect a given volume of an occupied space to be protected . although the unit 210 can be sized sufficiently to add a large number of such units to protect a very large space , for very large compartments , multiple units 210 spaced throughout the compartment , may be warranted to provide better mixing and inert gas coverage in the room . fig6 is an illustration of a ceiling mounted fixture , holding multiple gas generator cartridges , a ceiling fixture 310 is mounted on the ceiling , extending a short distance below the ceiling height . multiple gas generator units 320 can be mounted into the fixture at various bracket locations 330 , much like the mounting brackets for individual fluorescent light bulbs . like the system in fig5 , a varied number of units 320 can be added to the fixture 310 to vary the quantity of inert gas produced , and adjust for the room capacity to be protected . the fixture 310 can be sized to hold a certain maximum number of units 320 , corresponding to a maximum room volume , or floor space for a given ceiling height , that can be protected with one fixture ; beyond this room volume , additional fixtures would be added , spaced evenly throughout the room . as an additional option , the traditional room smoke detector 340 can be mounted into the fixture 310 , such as in its center , to activate the units 320 directly within the fixture 310 . in this manner , the electrical power wires applied to the detector can also be used to fire the squids of the units , rather than a remote routing of the power and detector lines , and the expense of routing an additional power line above the ceiling . the fixture 310 is covered with decorative dust cover 350 that hides the units and fixture with an attractive cover that blends into the ceiling motif , and features exhaust holes 360 around its perimeter functioning as a diffuser to direct the inert gas 370 discharged by the units into the room . such a location and manner of discharge of the system promotes effective mixing with the room air and gives maximum distance for the hot inert gas to cool before coming into contact with occupants below . the location on the ceiling permits the system to require no floor space or room location for mounting , thereby not impeding any activities or usage of the room . fig7 is an illustration of a ceiling mounted fixture , comprised of multiple recessed gas generator units . this unit is virtually identical to the system disclosed in fig6 , except this variant exploits the presence of a drop ceiling common to many business and computer rooms , or any other ceiling configuration that permits the mounting of the gas generator units 410 above the ceiling level . the units 410 are mounted to a ceiling cover 420 that is flush with the ceiling , with exhaust holes 430 present in the cover 420 to permit the diffusion and discharge of the inert gas 440 from the gas generator units 410 . this configuration has the advantage of having a flush - mounted ceiling unit , without any extension below the ceiling , in an even more discreet design . such “ in - room ” gas generator fire protection systems , with their local detection , power ( if supplied with back up power from capacitors or small batteries ) and discharge capabilities all present within the compartment , provides a robust protection system that is not impeded by power loss or loss of water pressure , or physical destruction of buildings or structures , or water mains ( which would also render water sprinklers unusable ) in the event of a catastrophic event at the facility in question , due to earthquakes or other natural disasters , explosions such as due to leaking gas mains , or even terrorist incidents , to continue to provide protection to critical compartments even if the rest of the facility is severely compromised . an illustration of a particular swing example will demonstrate the features of the configurations set forth in the alternative embodiments of fig4 - 7 . an oxygen concentration of 13 . 5 % is a desirable target level , to successfully extinguish fires with a sufficient 20 % factor of safety as required by regulatory agencies such as the national fire protection association , while maintaining sufficient oxygen levels for occupants for limited evacuation periods . prior testing of prototype gas generator units has shown successful fire extinguishment with units sized approximately 20 gallons in volume , producing 0 . 53 5 kg - moles of nitrogen inert gas , discharged into a 1300 cubic foot room , ar equivalent volume to be protected by one standard canister of traditional compressed stored inert gas . such a unit was not optimized in size in any respect , with copious and un - optimized quantities of cooling bed materials used to cool the discharged nitrogen gas . if such an un - optimized unit were prorated in size , including its oversized cooling bed capacity , it can provide a vastly conservative estimate of sizing on individual units and cartridges necessary when considering current art in gas generator technology and performance . the 0 . 535 kg - moles of gas can be increased to 0 . 6884 kg - moles to add the 20 % factor of safety required , to result in a 13 . 5 % oxygen concentration , which is still acceptable for occupants . sizing for protection for only 100 cubic feet of room space , a total of 1 . 483 kg of nitrogen is needed , rounded up to 1 . 5 kg . using the effective density of the tested unit , even with the un - optimized cooling bed , disc - shaped units of 24 inch diameter , and 1 . 5 inches thick , or rectangular units 4 inches thick by 9 inches wide and 18 inches long , can produce such quantities . either unit variant is calculated to weigh 23 . 4 lbs ., if scaling the previously tested 240 lb . unit . numerous disc shaped units can be stacked for the floor or wall - mounted model ; to protect the 1300 cubic feet space associated with a standard compress d inert gas canister , a unit 24 inches in diameter and 19 . 5 inches tall would be necessary ( taking very little space in the room ). such a unit could be increased in room capacity if needed by making it wider or taller ( theoretically up to the ceiling height ), but it may be alternatively preferred to add additional floor units in a large room for the ceiling mounted units , the aforementioned rectangular gas generator units could be employed . this would result in an extended fixture distance below the ceiling of the unit of just over 4 inches . the units that recess into the ceiling could be of approximately 10 inches in diameter and 8 inches tall . these individual units can be seen to be of a weight practical for an individual installation technician to lift and install into the overhead ceiling fixture . if such fixtures are designed to hold up to eight gas generator cartridges per fixture , to protect a ten by ten floor space if an eight foot ceiling is present , then even the total maximum fixture weight of 187 lbs . is practical for mounting to ceiling joists ( and less than some ornate lighting fixtures ). the individual gas generator units would be designed to discharge their gas along opposite sides along their length through multiple orifices , with such a configuration canceling any thrust loads otherwise possible . such eight - unit fixtures would only take the ceiling space of about three foot by three foot , including space between the gas generator units for gas to discharge and flow , which is roughly equivalent in area to two common ceiling tiles . the oxygen concentration will only fluctuate in an 800 cubic foot space of less than 1 % as one adjusts and adds each additional discrete gas generator unit to adjust for extra room capacity , which is certainly an acceptable tolerance level . in addition , one or two of the additional individual gas generator units can be used under the subfloor of common computer rooms , to provide required fire protection in those spaces as well . having a standard size for the cartridges works in favor of reducing the cost in gas generator production , by making many units of one size . if gas generator propellants and units continue to be optimized in the future , individual units as small as 4 inches by 2 . 5 inches by 5 inches , and a weight of 3 . 3 lbs . are possible , and full eight - unit ceiling fixtures could fit within a 12 inch square with a four inch thickness , and a weight of 26 . 5 lbs . fully loaded , if unit efficiencies near 100 % are approached . there is thus described novel techniques and features to improve the performance of fire extinguishing systems for occupied spaces employing solid propellant gas generators , which meets all of the objectives set forth herein and which overcomes the disadvantages of existing techniques . the many features and advantages of the invention are apparent from the detailed specification and , thus , it is intended by the appended claims to cover all such features and advantages of the invention that fall within the true spirit and scope of the invention . further since numerous modifications and changes will readily occur to those skilled in the art , it is not desired to limit the invention to the exact construction and operation illustrated and described , and accordingly all suitable modifications and equivalents may be resorted to , falling within the scope of the invention .
a method and apparatus for suppressing a fire utilizing non - azide solid gas propeilant generation to produce and transport a suitable gas for suppressing a fire in a normally occupied area . the nitrogen gas produced by the solid propellant gas generation is optionally treated to remove undesirable elements such as water and / or carbon dioxide from the product gas prior to the delivery of the product gas to the protected hazard area .