CA2250325C - Fire-extinguishing composition, fire extinguishing method and apparatus - Google Patents

Abstract

The disclosure relates to a method of extinguishing fires, a fire-extinguishing compound and a fire-extinguishing system. The proposed method involves the preparation of a fire-extinguishing composition containing an oxidant and a fuel-binder, placing the composition in the area of the seat of the fire, initiating a sustainable fuel oxidising reaction producing combustion products in finely dispersed aerosol form, and then allowing the aerosol medium to act on the seat of the fire.
According to the invention, the compositions in the aerosol products of combustion act in the immediate area of the fuel oxidation reaction to reduce the level of toxins and lower the equilibrium temperature of complete oxidation of the fuel-binder combustion products. To achieve this, a reagent is introduced into the aerosol combustion products of the composition which promotes a reduction in the equilibrium temperature of the full oxidation reaction of the fuel-binder combustion products. The reagent used consists of thermal disintegration products of a low-energy supplementary fuel. Also proposed is a compound suitable for the proposed method. The system is provided with a reactor containing means for reducing the level of toxins in the area of combustion of the composition.

Description

Fire Extinguishing Composition, Fire Extinguishing Method and Apparatus Field of the Invention The invention relates to aerosol-forming fire-extinguishing means and may be used for suppressing the seat of fire in closed and open spaces and preventing the explosion of vapors and aerosuspensions of flarnmable liquids, combustibles, and materials.
Prior Art Of all fire-extinguishing methods, the use of aerosol forming fire-extinguishing compounds is most promising. This is due to the fact that this method involves an efficient flame-suppressing mechanism where, when the dispersed phase of aerosol enters the seat of the fire, the chain reaction of active radicals (active centers) forming in the fire area is broken. In this re:'pect, each airborne particle absorbs the energy released in a recombination reaction involving active radicals, which, combined with their precipitation on the surface of airborne particle, results in an energy '°deficiency'° preventing the formation of new active radicals in the fire area. As the size of airborne partiicles decreases, the fire-extinguishing performance of their dispersed phase improves due to an increase in the total effective surface area of airborne particles and the consequent increase in the amount of active radicals retained by this surface.
The action of airborne particles on active radicals in the fire area terminates the spread of the chemical reaction, and the gaseous phase of aerosol inhibits flame by diluting it, which also results in its suppression.
An aerosol medium may be formed by igniting a pyrotechnic composition consisting of components which either form gaseous-phase combustion inhibitors, together with a dispersed medium in the combustion process, or are themselves the combustion inhibitors. The solids or condensed liquids of the dispersed phase which are released during combustion contain salts, oxides, or hydroxides of, for example, alkali or alkali-earth metals, which considerably improves the fire-extinguishing performance of the aerosol's condensation phase.
Most fire-extinguishing methods involve common operations, namely: placing the aerosol-forming composition in the area of the seat of the fire, initiating (upon the occurrence or detection of the fire's flame) a sustainable combustion of the composition, producing products in a finely dispersed aerosol form, and then allowing the aerosol medium to act on the seal: of fire.
The method of extinguishing fires in bulk by using the above operations is already known (SU, a.c. No. 1741816. A62G 2100, "1992). With this method, the composition produces toxins and high-temperature products during the process of combustion, which restricts the application of the method to extinguishing to spaces without people and makes the method unusable in the conditions of, for example mines, stores, offices, vehicle cabins, etc. wherein fire-extinguishing devices are activated when people are close to the seat of the fire. In addition, with no cooling means provided, this method requires a considerable increase in the concentration of the combustion products of the aerosol-forming composition to ensure that the fire is extinguished, which makes this method impractical for fire-extinguishing in open spaces.
The method whereby fires are extinguished by placing, in a protected space, the aerosol products forming in the combustion of tt~e pyrotechnic composition, in which the dispersed phase contains the salts of alkali or transition-group metals, and being cooled both in and outside the fire area is already known (SU, a.c. No. 2008045, A62C 3/00, 1994). The aerosol products are cooled by introducing a coolant which, in the fire area, appears as the thermal disintegration products of the lining of the reactor containing the pyrotechnic composition. For the coolant outside the fire area, an aerial or liquid coolant is used. The presence of the salts of alkali or transition-groin metals in the aerosol products of combustion improves the fire-extinguishing performance of the condensed phase of aerosol, as compared with the previous example, but the inefficient means of cooling and the resulting high temperature of the combustion of the pyratechnic composition both prevent reducing considerably the temperature of the aerosol products arriving at t;he seat of the fire, thereby reducing their fire-extinguishing concentration. Furthermore, the high level of toxins in the products of the composition combustion prohibits using this method in closed spaces in the presence of people, just as in the previous example.
The above fire-extinguishing methods make use of an aerosol-forming composition containing an oxidant, fuel-binder, and additives. However, the composition's formula does provides neither for an acceptably low temperature for the aerosol medium forming in composition combustion nor a satisfactorily low level of toxins to extinguish fires in closed spaces.
Of the aerosol-forming compositions for fire-extinguishing in the required conditions, the most suitable one is that including a supplementary fuel whose thermal disintegration products absorb energy released in fuel-binder oxidation and thereby cause the composition's combustion temperature to decrease somewhat (WO 92117244, A62~ 1100, 1992). In the process of the composition's combustion, toxins such as CO, NH3 and HCN form due to the *.
incomplete oxidation of the fuel, which restricts using that composition as the fire-extinguishing compound. Furthermore, the ambient air further oxidizes some of the incomplete products of oxidation, which causes the temperature of the aerosol jet acting on the seat of the fire to increase and consequently reduces the effectiveness of the flame suppression.

-4.
The previous example also provides a fire-extinguishing system which includes a reactor for the placement and combustion of the above aerosol-forming composition and its ignition, That system, however, lacks a means for lowering the level of incomplete-combustion toxic products ire the reactor, and so the aerosol jet emitted from the reactor heats up in the air through further oxidization of the incomplete-combustion products. To avoid this, the system must be used in combination with means to cool the: aerosol jet, supplementary units including a gaseous-type or water cooler, for example for cooling the aerosol jet, which complicates fire-fighting operations and impairs the fire-extinguishing performance of aerosol-forming composition.
EP-A-0 637 458 corresponding to RU-C-2046614, discloses a method for producing a fire-extinguishing composition comprising oxidant and fuel-binder.
The composition is placed in the area of the seat of the fire and on ignition produces combusion products in aerosol form.
DATABASE WPI Section PQ, Week 9541 Derwent Publications Ltd., London, GB; Class p35, AN 95-319363 XP002100347 & SU 1 821 985 A (FIRE
FIGHTING RES INST), 20 March 1995, discloses a fire-extinguisher having a combustion chamber containing a composition comprising oxidant and fuel-binder, contained in a perforated metal cup. The composition extinguishes the fire when ignited.
DE 94 16 112 U discloses compositions which may be used for extinguishing fires and comprising oxidant and fuel-binder. The compositions produce reduced levels of toxins following combusion.
Disclosure of the Invention It is an object of the present invention to develop a group of technical solutions to ensure that fires are extinguished efficiently and environmentally safely using the aerosol medium, in both closed and open spaces.
According to the invention there is provided a fire-extinguishing composition comprising the following components in weight %:
1.5 to 18% of fuel-binder selected from 4-oxybenzoic acid alone or in admixture with polymers, resins, elastomers;
3.0 to 25% of supplementary fuel selected from low-carbon or carbon-free polynitrogen compounds or organic or inorganic azides;
0.5 to 10% of additives selected from aluminium or magnesium, or their alloys, or catalytic additives including oxides of copper, iron zinc, manganese and chromium; and the remainder being oxidant.
The objective is achieved due to the fact that in the method involving the preparation of a fire-extinguishing composition containing an oxidant and fuel-binder, placement of the composition in the area of the seat of the fire, initiating a sustainable fuel-oxidizing reaction producing combustion products in finely dispersed aerosol form, and then permitting the aerosol medium to act on the seat of the fire, according to the invention, in the immediate area of the fuel oxidation reaction, the level of toxins in the aerosol products of composition combustion is reduced and, simultaneously, the equilibrium temperature for complete oxidation of the fuel-binder combustion products is lowered.
The level of toxins in the aerosol products of the cornbustion of the composition may be reduced by introducing a reagent which concurrently promotes a reduction In the equilibrium temperature of the full oxidation reaction of the fuel-binder combustion products.
It is appropriate to cool the aerosol products of the composition's combustion prior to their action on the seat of the fire, this being achievable outside the area of the fuel oxidation reaction.
In some actual cases, it is appropriate to feed the part of the aerosol products of composition combustion into supplementary fire-extinguishing means to force, for example, a fire-extinguishing agent in the form of a liquid, gas, or powder out of reservoirs containing such agents so that this agE:nt is fed into the seat of fire.
For the reagent promoting a reduction in the equilibriurr~ temperature for a full oxidation reaction of the fuel-binder combustion products, the thermal disintegration products of the low-energy supplementary fuel which is introduced to the fuel-binder at the composition preparation stage may be used.
This supplementary fuel may be introduced separately, or in combination with carbolic acid derivatives, or as a mixture including polymers, resins, and elastomers, in the form of individual components and their mixtures.
4-Oxybenzoic acid is used as the fuel-binder and low-carbon and carbon-free polynitrogen compounds or organic or inorganic azides as the low-energy supplementary fuel. The azides used are azodicarbonate, guanidine, dicyanodiamide, melon, melamine, urea, urotropin, azobisformamide, semicarbazide, dihydroglyoxime, tetrazole, ditetrazole, and their derivatives, or their salts or blends.
For the oxidant, it is appropriate to use nitrates or perchiorates of alkali metals, The objective of the invention is achieved further by the fact that, according to the invention, the fire-extinguishing compound consisting of the oxidant, fuel-binder, and additives also includes the supplementary fuel, promoting a reduction in the equilibrium temperature for the complete oxidation of the fuel-binder combustion products.
Low-carbon and carbon-free polynitrogen compounds or organic or inorganic azides such as azodicarbonate, guanidine, dicyanodiamide, melon, melamine, urea, urotropin, azobisformamide, semicarbazide, clihydroglyoxime, tetrazole, ditetrazole, and their derivatives, or their salts or blends with varying ratios may be used as the low-energy supplementary fuel for the compound.
In all cases it is appropriate to use nitrates or perchlorates of alkali metals as the oxidants in the preparation of the composition, due to their low price.
The composition also contains the following metals as additives: aluminum and magnesium, individually or their blends or alloys; in this respect, the latter may incorporate also the metals of 1ST and 2"d groups of i:he periodic table, copper, iron, and metal hydrides. It makes sense additionally to incorporate catalytic and processing additives in the form of oxides of copper, iron, zinc, manganese or chromium in the compound. The objective of the invention is further accomplished due to the fact that, according to the linvention, the fire-extinguishing system containing a reactor for the placement in the fire-extinguishing composition containing the oxidant and the fuel-binder, the ignition that initiates the compos;tion°s combustion ~>roducing the combustion products in the form of finely dispersed aerosol acting on the seat of the fire is provided with means installed in the reactor and intf:nded to reduce the level of toxins in the area of the composition's combustion, .and this ignition is implemented so as to be in thermodynamic interaction with the seat of the fire and thereby to ignite the composition automatically in cases of ambient temperature increase caused b~ fire, with the possihility of implementing the above means for reducing the level of toxins in the area of the composition's combustion in the form of the reactive-type reactor component promoting a reduction in the equilibrium temperature for complete oxidation of the fuel-binder combustion products.
The fire-extinguishing system may be equipped with means for cooling the aerosol products of the composition's combustion pirior to their action on the seat of fire, with the possibility of arranging these cooling rrteans outside the area of the fuel oxidation reaction. It is also appropriate to equip the fire-extinguishing system with means for feeding a part of the aerosol products of composition combustion into the supplementary fire-extinguishing means to force, for example, a tire-extinguishing agent in the form of liquid, gas, or powder out of the reservoirs containing such agents so that this agent is fed into the seat of fire.
The low-carbon and carbon-free polynitrogen compounds or organic or inorganic azides such as azodicarbonate, guanidine, dicyanodiamide, melon, melamine, urea, urotropin, azobisformamide, semicarbazide, dihydroglyoxime, tetrazole, ditetrazole, and their derivatives, or their ;>alts or blends are appropriate for the low-energy supplementary fuel.
The above features relate to technical solutions composing a single group being characterized by the underlining common objective of the invention and are essential due to fact that each of these features influences the relevant technical result which, in combination with other technical solutions, ensures the accomplishment of the invention's objective.
Thus, reducing the level of toxins in the aerosol products of the composition's combustion in the immediate area of the fuel oxidation reaction ensures not only the formation of an aerosol improved toxicological properties of combustion products, but a reduction in the temperature of the aerosol jet acting on the seat of the fire as well. This is due to the fact that reducing the level of toxins in the combustion products of the aerosol-forming composition decreases the temperature to which the aerosol jet heats up after leaving the area of the fuel oxidation reaction, through further toxin oxidation in the air. By simultaneously lowering the equilibrium temperature of the full oxid<~tion reaction of fuel-binder combustion products, the process of the flame oxid<~tion of the aerosol-forming composition may be converted into a stage of nonfl;ame~ gasification, or, at least, the dimensions of the flame area of the fuel-binder oxidation reaction may be decreased with a resulting improvement in the fire-extinguishing performance.
Used in the implementation of the method, the compound that contains a supplementary fuel which promotes a reduction in tlhe equilibrium temperature of the full oxidation reaction of the fuel-binder combustian products, the compound components in the above-mentioned weight ratio allow a reduction in the level of toxins in the resultant aerosol by further oxidizing the incomplete-combustion products of the fuel-binder in the immediate area of the reaction.
As a result, the level of toxins in the aerosol jet entering the seat of the fire is reduced, promoting a reduction in the temperature i:o which the jet heats up due to further oxidation of the toxins by atmospheric oxygen. Furthermore, selecting the type of supplementary fuel makes it possible to decrease considerably the lower limit of the fire-extinguishing concentration of aerosol and thereby ensure an acceptable rate of consumption for the aerosol-forming compound when extinguishing open fires.
Used as a supplementary fuel, separately or in combination with the fuel-binder, low-energy fuel permits the intensification and control of the compound's combustion process and, as a result, an increase in the outflow of the finely dispersed portion of gas-aerosol mixture produced by combustion, which results in improved fire-extinguishing performance by the c~ampounds and a reduced temperature for their combustion.
Using low-carbon or carbon-free palynitrogen compounds, such as dicyanodiamide, in the low-energy supplementary fuel permits the combustion process to achieve, simultaneously, improved fire-extinguishing performance, further decreases in combustion temperature, and k~etter oxidation of combustibles, i.e., to ensure a further decrease in the toxicity of combustion products.
Used as oxidants, nitrates or perchlorates of alkali rnetals like potassium and sodium or their blends in compounds containing low-energy supplementary fuel in combination with carbolic-acid derivatives promote the formation of K20, Na20, KOH, NaOH, K2C03, Na2C03, KCI, NaCI, and similar solid particles in combustion products and further improve the fire-extinguishing performance of the aerosol component of the compound combustion products. Using such oxidants produces combustion products with a higher content of inert gases like nitrogen and carbon dioxide, which further improves the compounds and fire-extinguishing medium in their fire-extinguishing performance and toxicological properties, respectively.
When introduced to the fuel-binder, the polymers, rEains, and elastomers in diverse combinations with 4-oxybenzoic acid improve the cohesive bonds between the compound particles, allowing the fabrication of large-size units with a capacity up to and exceeding 100 kg. In this respect, the strength of the units is considerably improved.
Contained in the fire-extinguishing compounds, metal additives like aluminum and magnesium in the form of individual componenlts or their mixtures or alloys - and the latter may also incorporate the metals of the 1St and 2nd groups, such as copper, iron, and metal hydrides - permit an increase in the flammability of compounds and a controllable rate of compound combustion.
The introduction tc the composition of processing additives improves its flow properties, and the catalytic additives in the form of copper, iron, zinc, manganese, chromium oxides improve the toxicological properties of combustion products, that is, contribute t~ decreasing the CO, NH3, HCN levels in these products.

The proposed fire-extinguishing system, which incorporates a reactor in which the fire-extinguishing composition and the means for reducing the level of toxins in the area of combustion of the composition are pl<~ced may treat both enclosed and open fires. Implementing the ignition o as to enable it to be in thermodynamic interaction with the seat of the fire permits self-activation of the system in fire, thereby improving its fire-extinguishing performance.
The invention will now be described with reference to the table containing the experimental investigation results for the proposed compound and the most similar prior-art compound at to their fire-extinguishling performance, combustion temperature, and the levels of toxins.
Corroboration of the Invention's Feasibility The fire-extinguishing method is implemented as follows:
First, the aerosol-forming fire-extinguishing composition is prepared in the sequence of required operations to ensure the necessary aggregate state of the composition. Thus, to prepare the composition charge of solid-phase fuel, the powder components, including the oxidant for which nitrates or perchlorates of alkali metals are preferably used, and the fuel binder are ground and blended, then the component mixture is compacted using thE~ so-called "blind" method to obtain a charged cartridge in the required shape, To prepare the liquid- or thickened-phase composition, the component mixture is dissolved in the liquid agent, adding thickeners, as required. The aggregate state of the composition is chosen depending on the way its being placed in the area of the seat of the fire.
Thus, if being placed in a protected area beforehand, the composition may be used in any of the above-mentioned aggregate states. If placed in the seat of an incipient fire by, for example, throwing the composition towards the seat, a composition prepared in a thickened state is preferable.

-'I 2-Once the composition has been prepared and placed in the seat of the fire, the sustainable oxidizing reaction which produces the combustion products in aerosol form is initiated in the composition fuel. The fuel oxidizing reaction may be initiated remotely by effects occurring in the seait of fire; which is preferable for fire-extinguishing in closed spaces where the initiating function is performed by the temperature increase sensed by the fire-extinguishing device which is placed in the protected space beforehand. if thrown towards the seat of fire, the composition may be ignited at various points in the trajectory, including those within the space of fire and above it.
In the composition's combustion, its fuel-binder oxidizes, producing combustion products in aerosol form. Due to incomplete fuel oxiidation, the gaseous phase of aerosol contains toxins, mainly in the form of carlaon monoxide, ammonia, and cyanides, which oxidize further in air and thereby increase the temperature of the fire-extinguishing medium acting on the seat of the fire. To avoid this undesirable effect, the level of toxins in the aerosol products of the composition's combustion is reduced in the immediate area of the fuel oxidation reaction and, simultaneously, the equilibrium temperature of the full oxidation reaction of the fuel-binder combustion products is lowered. The latter operations cause the heat released in composition's combusticm to decrease considerably, resulting in toxicologically improved reduced-temperature aerosol fed in the fire area.
Reducing the level of toxins in the aerosol products resulting from the composition's combustion is achievable in various ways, for example, by introducing a reagent promoting a reduction in the equilibrium temperature of the full oxidation reaction of the fuel-binder combusltion products. In doing so, the level of toxic carbon-monoxide in the aerosol is reduced by terminating the fuel oxidation reaction, with the involved carbonic-core formation process leading to an acceleration in the oxidation of carbons monoxide. The level of other toxins is reduced through chemical reactions proceeding between the reagent and the other components of fire-extinguislling composition at the lowered temperature of its combustion.
For the reagent promoting a reduction in the equilibrium temperature of the full oxidation reaction of fuel-binder combustion producas, the thermal disintegration products of low-energy supplementary fuel introduced in the fuel-binder at the composition preparation stage are suitable. Then the energy released in the area of fuel oxidation reaction goes into the disintec,~ration of the low-energy supplementary fuel, resulting in a reduced temperature for the composition's combustion. Further chemical reactions between the thermal disintegration products of the low-energy supplementary fuel and the fire=extinguishing composition products lead to the formation of nontoxic products of combustion.
Low-carbon and carbon free polynitrogen compounds, for example, dicyanodiamide, melon, melamine, urea, urotropin, are suitable as low-energy supplementary fuel. With such supplementary fuel used, introducing additionally, in the compound of above-mentioned reagent, the combustion products of carbolic acid derivatives, for example 4-oxybenzoic acid, as well as polymers, resins, and elastomers which may be incorporated as individual components, or their blends in the fuel-binder resulits in an improvement in, as compared with the most similar previous method, the fire-extinguishing process in respect of all three aspects, namely: fire-extingui:;hing performance, combustion temperature, and the level of toxins, as shown the table attached herein.
The aerosol entering the seat of the fire covers the fire area and comes in contact with the flame, resulting in the realization of the previously described mechanism of suppressing the physical and chemical processes of combustion.
Reducing the aerosol temperature through feeding 'the reagent facilitating a reduction in the equilibrium temperature of the full oxidation reaction of fuel-binder combustion products, into the area of fire-exltinguishing composition combustion, permits improving further the fire-extinguishing system performance through feeding a part of the aerosol products of the composition's combustion into the supplementary fire-extinguishing means to force the fire-extinguishing agent in the form of liquid, gas, or povvder out of reservoirs containing such agents so that this agent is fed into the seat of fire.
The temperature of the aerosol leaving the area where it forms is sometimes sufficiently low to permit efficient fire-extinguishing. 1n such cases, the aerosol products of the composition's cambustion may be cooled prior to action on the seat of the fire. Cooling in such cases is preferably iimplemented outside the area of the fuel oxidation reaction by, for example, introducing water or brine to the aerosol.
The proposed fire-extinguishing method may be realized by using as the fire-extinguishing composition a compound consisting of the oxidant, fuel-binder, additive, and supplementary fuel, facilitating a reduction in the equilibrium temperature of the full oxidation reaction of the fuel-binder combustion products, with the above components being used in the following ratios, mass %:
fuel-binder 7 .5 to 18 supplementary fuel 3.0 to 25 additives 0.5 to 10 oxidant the remainder For the supplementary fuel in the compound, the low-energy fuel may be used separately or in combination with the fuel-binder component. Low-carbon and carbon-free polynitrogen compounds or organic or iinorganic azides such as azodicarbonate, guanidine, dicyanodiamide. melon, melamine, urea, urotropin, azobisformamide, semicarbazide, dihydraglyoxime, tetrazole, ditetrazole, and their derivatives, or salts are may be used as low-energy fuel for the compound.
Nitrates or perchlorates of alkali metals are used for the oxidant in the compound in all cases of its preparation.
For the additives to the compound, metals - aluminium and magnesium in the form of individual components or their blends or alloys; in this respect, the latter may additionally include the metals of the 1St and 2~'d groups, such as copper, iron and metal hydrides - are used. The compound may also contain processing and catalytic additives in the form of oxide of copper, iron, zinc, manganese or chromium.
The grounds for establishing the ranges for the above component content are shown in the attached table. The first column of the table provides a list of substances used in the proposed fire-extinguishing compound and divided into the groups relating to the oxidant, fuel-binder, the supplementary fuel which promotes a reduction in the equilibrium temperature; of the full oxidation reaction of the fuel-binder combustion products, processing,and catalytic additives.
The lower items in the column contain the following names - fire-extinguishing performance, combustion temperature, and the levE:l of toxins - of the performance of the fire-extinguishing process under examination. The second and further columns numbered 1 to 25 provide the mass percentage values for the content of specific components used in the fire-.extinguishing compound sample under testing and the values of fire-extinguishing process performance.
As evident from the table, using the fuel-binder in a mass ratio of less than 1.5 makes the test samples actually incombustible (r>ample 15), while increasing the fuel-binder weight ratio above 18 % impairs the fire-extinguishing performance of the compound (sample 16). Thus the proposed fuel-binders are applicable only in the ratios varying from 1.5 to 18.CI wt%.
The table data also give grounds for varying the mass content of supplementary fuel in the fire-extinguishing compound within only a limited range. Thus, with content below 3 mass % and above 25 mass %, the fire-extinguishing process performance on average does not exceed that of the most similar previous example (samples 17 and 18), while using the supplementary fuel in the fire-extinguishing compound in the ratio within the range of 3 to 25 mass improves this performance considerably (samples 1 to 14). Note that the fire-extinguishing process performances for samples 19 to 22 where the supplementary-fuel mass content of the fire-extinguishing compound does not fall outside the permissible range are far from satisfactory. However this result cannot call into question the validity of the established range of 4 to 23 mass %, as it relates to the compounds with a fuel-binder content falling outside the above-mentioned optimized range of 1.5 to 18.0 mass%. It is worth noting, as to the 0.5 to 10 mass % range established for the additives in the fire-extinguishing compound, that actually any point of this range corresponds to the fire-extinguishing process performances that are improved, compared with the most similar previous example (samples 2 to 5, 8, -11, 12). Below the lower limit of this range, a similar effect is accomplished for compounds with high content of low-energy supplementary fuel (samples 1, 6, 9, 10, 16), that is, within the non-optimized combination of components. Exceeding the upper limit of the established range impairs the ignition of the fire-extinguishing compound.
As for the oxidant content of the compound, it has keen shown experimentally that the ratio may vary for the oxidants of nitrates oir perchlorates of alkali metals. The ratio affects only the applicability of compounds. Thus, with a higher level of chlorides in the aerosol, the compound is more suitable for extinguishing class A fires and, with increased content, it may be used for extinguishing class B fires.
The analysis of table data shows that;
- the test compounds surpass the most similar previous example in fire-extinguishing performance;
- the test compounds feature a lower combustion temperature than that of the most similar prior example;
- the combustion products of test compounds have better toxicological properties (decreased content of CO, NH3, HCN) than those of the most similar previous example).
The above results show that using the fire-extinguishing composition of said formula truly promotes a reduction in the equilibrium temperature of complete oxidation of the fuel-binder combustion products, this technical solution being accomplished by introducing to the fire-extinguishing composition a supplementary fuel with the above-described properties.
The essence of the invention, in respect of the composition, is explained with reference to the samples of its preparation.
Example 1 Composition, mass % sodium nitrate 68 4-oxybenzoic acid 17 urea 15 68 g of sodium nitrate, 17 g of 4-oxybenzoic acid, 15 g of urea are transferred to a mixer. The blend is mixed for 1 hour. The cartridges of required shape are molded using the resultant mixture through "blind" molding under the specific _18_ pressure of 1500 kgflcm2.
Example 2 Composition, mass % epoxy resin 5 potassium nitrate ~0 4-oxybenzoic acid 10 dicyandiamide (DCDA) 14 industrial oil 1 70 g of potassium nitrate, 10 g of 4-oxybenzoic acid, 14 g of DCDA are transferred to a mixer and the blend is mixed for 10 to 15 minutes. Then 5 g of epoxy resin and 1 g of processing additives (in this case, the industrial oil) are added. The blend is mixed for 15 to 20 minutes. The cartridges in the required shape are molded from the resultant mixture using the hydraulic press under the specific pressure of no less than 1000 kgflcm2 and are then cured for 24 hours at 40 to 50 °C.
Example 3 Composition, mass % potassium nitrate 60 sodium nitrate 8 4-oxybenzoic acid 9 phenol-formaldehyde: resin 8 dicyandiamide (DCD,A) 12 Cu~ 2 fluoroplastic-4 1 The process of preparation is similar to that in example 1.

Fire-extinguishing performance (FEP, glm3), combustion temperature (Tc, °C), the levels of CO, NH3, HCN in the combustion products were estimated based on the samples fabricated using "blind" molding.
Testing the compounds for the fire-extinguishing performance was performed using the following procedure. The weighed portion of the test compound was combusted in a dosed space (0.04 m3). After distributing the aerosol over the volume for 60 seconds, a burning sample of polymethyl methacrylate (organic glass) was introduced to the area. Upon the set of tests with various quantities (the weighed portions) of test compound, its minimuim weighed portion after combustion of which the organic glass burnt in the volume for at least 1 s was determined. The minimum fire-extinguishing concentration for the test compound was determined by division of the minimum weighed portion by the volume.
The temperatures of the compodnd's combustion were determined using a contact thermoelectric method, with chromel-alumel thermocouples. The thermojunction diameter of the thermocouples used was 100 pm Analysis for toxic products - CO, NH3, HCN - in the combustion products of compounds was performed using a chromatograph with a heat conduction detector. Chromatographic column: glass, packing type, 2.4 m in length, 2.5 m in internal diameter. Stationary phase: zeolite of 0.14 to 0.25 mm fraction.
Carrier gas (helium) flow: 30 cm3lmin. Column temperature: 32°C.
Injection volume: 1 cm~. The chromatograms were recorded with a TLI-4601 recorder.
The following fire-extinguishing system was used for the implementation of the method invented.
The system includes a reactor far the placement of ithe fire-extinguishing composition which consists of the oxidant and the frael-binder. The composition is fired by the ignition to give the combustion products a finely dispersed aerosol form. In addition to the oxidant and fuel-binder, the reactor contains the means to reduce the level of toxins forming in the area of the composition's combustion. The ignition is implemented so as to be in thermodynamic interaction with the seat of the fire and thereby to ignite automatically the composition in case of ambient temperature increase caused by fire. This thermodynamic interaction may be implemented in 'the form of various-design devices, for example, in the forrrai of a temperature sensor with an actuator, including the fire-extinguishing composition ignition and provided with a disabler to disable, if required, the thermodynamic interaction and to allow remote ignition of the composition by command or manually.
The means for the reduction of the level of toxins forming in the area of the composition's combustion may be implemented in tile form of the reactive-type reactor component promoting a reduction in the equilibrium temperature of the complete oxidation of the fuel-binder combustion products, and, for the reactive-type reactor component, the low-energy supplementary fuel may be used either separately or in combination with 4-oxybenzoic acid, and the low-energy supplementary fuel may involve low-carban and carbon-free polynitrogen compounds or organic or inorganic azides such as <~zodicarbonate, guanidine, dicyanodiamide, melon, melamine, urea, urotropin, azobisformamide, semicarbazide, dihydro-glyoxime, tetrazole, ditetrazole, and their derivatives, or their salts or blends.
The system operates in the following manner.
If intended to extinguish fires in closed spaces, the system is placed in a room beforehand and, in case of fire, activated automatic,aily or by command from a common room-security station. The temperature increase in the protected space automatically enables the mechanism of thermodynamic interaction with the seat of the fire, initiating thereby the sustainable combustion of the composition producing combustion products in the 'form of a finely dispersed aerosol which enters the seat of the fire and suppresses the flame. The aerosol may be fed to the seat of the fire using various methods, for example, through aerosol outflow occurring across a part of or the entire surface of reactor, which results in the distribution of the aerosol over the entire protected space.
Alternatively, the aerosol may flow out of the reactor through a pass in the form of a nozzle, resulting in a directed jet which will have an additional blowing action on the seat of fire, due to ram pressure. The last alternative allows the aerosol to be cooled in a simpler way, for example, by injecting coolant (water and other fire-extinguishing liquids) into the jet.
In process of the composition's combustion, the means provided in the reactar to reduce the level of toxins in the fire area are activated. ULlith these means implemented in the form of a reactive-type reactor component promoting the reduction in the equilibrium temperature of the complete oxidafiion of the fuel-binder combustion products, the toxicologically improved and cooled aerosol, which poses no hazards to persons in the protected space, leaves the reactor and, depending on temperature requirements, may be partially fed into the supplementary fire-extinguishing means to force the fire-extinguishing agent -in the form of liquid, gas, or powder - out of reservoirs containing such agents so that this agent is fed into the seat of the fire.
Using, as the reactive-type reactor component, low-energy supplementary fuel both separately and in combination with carbolic acid derivatives, polymers, resins, and elastomers, or their blends, that is, with low-cost and available materials, provides the simplest approach to manufacture a fire-extinguishing system with the required properties, while the use of 4-oxybenzoic acid as the carbolic acid derivative, and low-carbon and carbon-free polynitrogen compounds or organic or inorganic azides as the low-energy supplementary fuel improves the performance of this system.
Industrial Use The above-disclosed method, compound, and system for extinguishing fires may be successfully used to suppress flames where gaseous, liquid, and solid combustibles are ignited in stationary rooms, on railway and motor vehicles, river and sea vessels, aircraft, to prevent explosions in spaces containing methane-air mixture, for example, in mines, as well as to extinguish fires in large open areas. The method is proven on articles up to 100 kg and more in mass and on sets of systems arranged as thermodynamically linked systems or looped with electric cables.

Table Composition (wt Prototype1 2 3 4 5 6 7 8 9 %) and ro erties Oxidant: KNOB 70 68 73 68 70 60 60 60 68 NaNOs 8 34 KCIOa 8 34 NaCIOa 8 Fuel-binder 4-oxybenzoic acid 17 4 10 9 12 12 17 Phenol-formaldehyde11 6 8 5 5 8 resin Epoxy resin 5 5 5 Coolant: DCDA 19 19 20 14 12 Melem 15 Melamine 15 Urea 15 15 Urotropin 15 GDA

Processing additives 1 1 Catalyst: Cu0 4 3 FezOs 4 Zn0 K2Crz0~
-Mn02 Minimum value of fire- 25 14 16 20 18 20 17 18 19 16 extinguishing concentration, FEP, glm3 Combustion temperature, Tc,C 1000 850 920 950 860 800 870 950 960 850 Level of toxins, 730 210 180 340 210 300 280 220 250 250 pglm3 CO

NHs 70 42 35 54 30 44 38 35 42 43 a e~ n " m,u .,.. yinxn,.. Tx,. z.. .. , rrvWNAW Ntxne.,.-s. ,~:..~sy9lYFCMKm eP X~.'n ~k P A r r-~:;: epaq, mw,. ,.."-.d,ws".""...-<."" .w,N.usm. y w;.~,.~<o..mm~m. ~ "r,ws,..~ ....5,w~.,.",."",..,w........-----~»..w~~.",.,..,.".-r.,.~ .............~.".",.."",..,..~.,".~....n..._,_,.-..

Table (continued) Composition (wt 10 11 12 13 14 15 16 17 18 19 20 21 22 ~) and properties 68 68 68 68 73.5 74 65 76 62 90 60 Oxidant: KNOB

NaNOs 38 KCIOa 30 NaCIOa 30 38 Fuel-binder 4-oxybenzoic 6 6 6 6 1.5 1 9 6 9 5 17 18 9 acid 6 6 5 4 Phenol-formaldehyde resin Epoxy resin 6 5 6 5 5 3 3 3 5 Coolant: DCDA 10 9 20 20 5 20 Melem 9 4 25 Melamine 15 _ Urea 14 10 9 Urotropin 9 Processing additives Catalyst: Cu0 5 5 Fe20s 3 Zn0 2 K2Crz0~ 2 5 Mn02 4 Minimum value of 19 18 18 17 15 26 24 24 28 24 22 24 fire~xtinguishing concentration, FEP, g/m3 Combustion temperature, Tc,C 800 940 960 950 970 10501080 980 110 1050 920980 Level of toxins, pgim3 260 320 280 270 200 880 700 890 400 810 350380 CO

.. . _. ,eu.n , a, MW . . ,~., W,. e..m~.> x.,.ft~qmN.Y.wz ..,.
.;ezh'N4nri~.P..s, - :yAAIMNW.» " ,W.avrcpw.w ...,_ r~wM.ennmw.my -pms~
~e~2s...n....,.nwx«emM.m..var.,..n...-~.-.,_.~,.............a.~.._-............,.w.",.".v..,.~..K..~.,.......~_._.-..~-_w

Claims (15)

Claims

1. Fire-extinguishing composition comprising the following components in weight %:
1.5 to 18% of fuel-binder selected from 4-oxybenzoic acid alone or in a mixture with polymers, resins, elastomers;
3.0 to 25% of supplementary fuel selected from low-carbon or carbon-free polynitrogen compounds or organic or inorganic azides;
0.5 to 10% of additives selected from aluminium or magnesium, or their alloys, or catalytic additives including oxides of copper, iron, zinc, manganese and chromium; and the remainder being oxidant.

2. A composition according to claim 1, characterized in that the low carbon or carbon-free polynitrogen compounds comprise azodicarbonate, guanidine, dicyanodiamide, melon, melamine, urea, urotropin, azobisformamide, semicarbazide, dihydroglyoxime, tetrazole, ditetrazole, and their derivatives, or their salts.

3. A composition according to claim 1 or 2, characterized in that the oxidant comprises nitrates or perchlorates of alkali metals.

4. A composition according to any one of claims 1 to 3, characterized in that the alloys of aluminum and magnesium also incorporate the metals of first and second groups of the periodic table, copper, iron, and metal hydrides.

5. Use of a composition according to any one of claims 1 to 4 in a fire-extinguishing apparatus.

6. A fire-extinguishing apparatus including a reactor for the placement of a fire-extinguishing composition and means for producing combustion products of said composition in the form of a finely dispersed aerosol acting on the seat of the fire, characterized in that the fire-extinguishing composition according to any of claims 1 to 4 is installed in the reactor for reducing the level of toxins in the area of the composition's combustion, ignition being implemented so as to be in thermodynamic interaction with the seat of fire and thereby to ignite the composition automatically in cases of ambient temperature increases caused by fire.

7. An apparatus according to claim 6, characterized in that said means for reducing the level of toxins in the area of the composition's combustion are implemented in the form of a reactive-type reactor component which promotes a reduction in the equilibrium temperature for the complete oxidation of the composition combustion products.

8. An apparatus according to claim 6 or 7, characterized in that it further comprises means for cooling the aerosol products of the composition's combustion prior to their action on the seat of fire, with arranging these cooling means outside the area of the fuel oxidation reaction.

9. An apparatus according to any one of claims 6 to 8, characterized in that it further comprises means for feeding a part of the aerosol products of the composition's combustion into a supplementary fire-extinguishing means to force a fire-extinguishing agent in the form of liquid, gas, or powder out of reservoirs containing such agents so that said agent is fed into the seat of the fire.

10. A method of extinguishing a fire comprising use of a composition according to any one of claims 1 to 4.

11. A method of extinguishing a fire, comprising preparing a fire-extinguishing composition according to any one of claims 1 to 4, placing the composition in the area of the seat of the fire, initiating a sustainable fuel oxidizing reaction which produces combustion products in a finely dispersed aerosol form, and then allowing the aerosol medium to act on the seat of the fire, whereby, in the immediate area of the fuel oxidation reaction, the level of toxins in the aerosol products of the composition's combustion is reduced and, simultaneously, the equilibrium temperature for the complete oxidation of the fuel-binder combustion products is lowered.

12. A method according to claim 11, characterized in that the level of toxins in the aerosol products of the composition's combustion is reduced by introducing a reagent promoting a reduction in the equilibrium temperature of the full oxidation reaction of the combustion products of the composition.

13. A method according to claim 11 or 12, characterized in that the aerosol products of the composition's combustion, prior to action on the seat of the fire, are cooled outside the area of the fuel oxidation reaction.

14. A method according to any one of claims 11 to 13, characterized in that a part of the aerosol products of the composition's combustion is fed into supplementary fire-extinguishing means to force a fire-extinguishing agent in the form of liquid, gas, or powder out of reservoirs containing such agents so that said agent is fed into the seat of the fire.

15. A method according to claim 12 or claim 13 or 14 when dependent thereon, characterized in that, for the reagent promoting a reduction in the equilibrium temperature of the full oxidation reaction of the fuel-binder combustion products, the thermal disintegration products of the supplementary fuel which is introduced into the fuel-binder at the composition preparation stage are used.