Cast primer and small-diameter explosive composition and process for the manufacture thereof

Abstract: A solid explosive composition is made by curing a mixture of a from about 20% to about 50% by weight of a liquid matrix, from about 50% to about 80% by weight of a dry or monohydrate inorganic chlorate or perchlorate salt, and from 0% to about 22% of a salt selected from the group consisting of nitrate oxidizer salts and inert chloride salts, after transferring said mixture to a mold. The matrix can include from about 50% to about 84% by weight of a non-explosive liquid fuel selected from the group consisting of polyhydric alcohols, lower aliphatic alcohols, ketones, and hydrocarbons; from 0% to about 15% by weight of a nitrate oxidizer salt; from 0% to about 15% by weight water; from 0% to about 15% by weight of a thickener; from 0% to about 5% by weight of an acid; and from 0% to about 2% by weight of a surfactant.

Description: The present invention relates to a method of preparing a solid cast explosive product suitable for use as a primer and a small diameter explosive. The present invention further relates to an explosive product obtainable by the aforementioned process. With the advent of ammonium nitrate and fuel oil mixtures, known as ANFO, into the explosives industry in the early 1950's, and of other, lesser or more sensitive explosive mixtures since that time, ways were sought to develop an initiator for these materials in surface and underground blasting. As a result, there was developed a cast primer or booster. The cast primer is made from self-explosives such as trinitrotoluene [TNT], cyclotrimethylenetrinitramine [RDX], pentaerythritol tetranitrate [PETN], and mixtures thereof such as Composition B which contains about 60% RDX, 40% TNT, and some wax as desensitizer. The first cast products were made with a variety of sensitive cores such as PETN or a coiled detonation fuse. The known and presently used process for making such cast primers or boosters consists of melting the above mentioned sensitive explosives or combinations thereof, often at temperatures of 100°C or higher, and casting the melted explosive into molds. The greatest hazard posed by the operation is the risk that the temperature control means fail, and thus, the explosive may reach decomposition temperature and explode. Aside from this grave risk, the process is inherently dangerous in that self-explosives are being handled. These are subject to shock detonation even at lower temperatures. Furthermore, in handling the cast products, an extremely sensitive dust may be produced which is even more hazardous than the cast primer itself. For example, following shipment, pentolite primers have been observed to leave a residue of abraded, fine, particulate dust in their shipping containers. There are disadvantages other than the risk of explosion. The materials used are expensive and some are not available from domestic sources. The molds must, of course, be able to withstand the heat of the melted explosive. Nevertheless, such primers are widely used because they have the advantage of being relatively water resistant. Other combinations of primers and boosters based on water gel and/or emulsion based compositions may display only some water resistance or no water resistance at all. In the past, there have been attempts to formulate insensitive slurry or emulsion type explosives using aqueous solutions of inorganic chlorate and perchlorate salts, i.e., salts of either the chlorate (ClO 3 ) or perchlorate (ClO 4 ) anions. These inorganic chlorate and perchlorate slurries and emulsions have serious drawbacks. Their density has to be carefully controlled by using gases (as small bubbels), micro-balloons or similar inert, insensitive, materials that complicate processing and detract from the energy of the primers. GB-A-907,611 relates to a slurry blasting agent containing, as essential components and each in percent by weight of the slurry, a solid oxidant selected from inorganic chlorates and perchlorates and present in an amount in the range of 70% to 90%, a water soluble liquid fuel selected from methanol, ethanol, isopropanol, polyhydric alcohols like ethylene glycol, diethylene glycol, glycerol, ketones like acetone or methyl ethyl ketone and present in an amount in the range of 5% to 20%, and water in an amount in the range of 1% to 10%. Optionally, the solid oxidant may contain 0% to 70% ammonium nitrate by weight and the slurry may contain a hydrophilic colloid such as guar gum or starch for controlling the viscosity of the slurry. The slurry can be safely prepared by mixing the components; the slurry may be safely stored and shipped or prepared on site. US-A-3,695,948 relates to a cast explosive composition which is cast and cured at ambient temperature in the absence of a thickening agent and which contains as essential components, each in percent by weight of the explosive composition, an inorganic oxidizer salt including alkali, alkaline earth and ammonium chlorate or perchlorate in an amount in the range of 30% to 93%, thiourea in an amount in the range of 5% to 40%, and water in an amount ion the range of 2% to 20%. The mixture may optionally include up to 30% water-insoluble fuel in the form of petrolic liquid, e.g. fuel oil and crude oil fractions, up to 5% density controlling agent in the form of hollow glass microspheres, and up to 2% thickening or gelling agent for preventing settling of the slurry prior to casting. The constituents are just mixed and the resultant slurry solidifies upon standing to yield a stiff and hard body. US-A-3,390,029 relates to an inorganic oxidizer salt explosive composition containing organic fuel solvent for the salt. The explosive composition contains, as essential components and each in percent by weight of the explosive composition, an inorganic oxidizer salt selected from ammonium nitrate, sodium nitrate, potassium nitrate, calcium nitrate, ammonium perchlorate, sodium perchlorate and magnesium perchlorate and present in an amount in the range of 60% to 90%, an organic fuel in the form of a water soluble, polar solvent selected from, inter alia, glycol, lactic acid, glycolic acid, amides and organic carbonates and present in an amount in the range of 5% to 40%, and a cross-linking agent in an amount in the range of about 0.1% to about 1% for solidification. US-A-3,395,056 relates to an inorganic oxidizer salt-alcohol explosive slurry containing an alcohol thickening agent. The explosive slurry contains, as essential components and each in percent by weight of the slurry, an inorganic oxidizer salt selected from alkali, alkaline earth or ammonium nitrate, chlorate or perchlorate or mixtures thereof and present in an amount in the range of 10% to 95%, a lower aliphatic alcohol selected from the C 1 -to C 4 -alcohols and present in an amount sufficient for providing 75% to 125% of the oxygen balance, and water in an amount in the range of 1% to 10%. An alcohol thickening agent such as guar gum or its derivatives is added in an amount in the range of 0.1% to 3.0% so as to provide the required consistency of the slurry. The explosive composition is prepared by blending the solid materials and adding water and alcohol. US-A-3,684,594 relates to aqueous explosive compositions having reversible fluent-nonfluent properties. Specifically, the explosive composition contains, as essential components and each in percent by weight of the explosive composition, an inorganic oxidizer salt selected from alkali, alkaline earth and aluminum perchlorates and present in an amount in the range of 25% to 90%, and water in an amount in the range of 3% to 15%. Optionally, there are further added a metallic fuel like aluminum powder and an organic solvent capable of forming solvates with the inorganic oxidizer salt and selected from, inter alia, polyhydric alcohols, ethylene glycol, propylene glycol, polyethylene glycol, polypropylene glycol, the organic solvent being present in an amount in the range of 0% to 5.0%. For preparing the explosive composition, an amount of water sufficient to form a hydrate is added to the inorganic oxidizer salt at a temperature above the hydrate decomposition temperature, the other components are added to the thus obtained slurry at the aforementioned temperature and the slurry is, then, filled into a container and cooled below the hydrate decomposition temperature so that the slurry is solidified due to the formation of crystalline hydrate. It was a principal object in the making of the present invention to provide a castable primer explosive that would maximize borehole pressure (which is a function of both velocity and density), and that would use insensitive inorganic perchlorate salts, especially the relatively shock-insensitive sodium perchlorate, instead of self-explosives. Other objects were to be able to make a cast primer or booster at ambient temperatures and thus avoid the hazard of working with explosives at elevated temperatures; to provide a cast primer or booster that, during handling, does not produce sensitive and hazardous dust; and to make a cast primer or booster that increases in sensitivity after it is formulated and placed in a container so as to enhance the margin of safety in handling the explosive. With respect to the inventive method of preparing a solid cast primer, these objects are achieved by the following steps: (a) selecting a dry inorganic perchlorate salt from the group consisting of sodium perchlorate, potassium perchlorate, ammonium perchlorate and mixtures thereof, (b) selecting a dry inorganic nitrate salt from the group consisting of ammonium nitrate, calcium nitrate, sodium nitrate, potassium nitrate and mixtures thereof, (c) preparing a liquid matrix containing a water soluble oxygenated organic fuel of low volatility in an amount of 50% to 84% by weight, said water soluble oxygenated organic fuel being selected from the group of polyhydric alcohols consisting of glycerol, ethylene glycol, diethylene glycol, triethylene glycol, tetraethylene glycol, propylene glycol, dipropylene glycol, tripropylene glycol, still bottoms remaining from their purification and mixtures thereof, and further containing, each in percent by weight, a thickener in the amount of 0% to 15%, a nitrate salt in an amount of 0% to 22%, an acid in an amount of 0% to 5%, and water in an amount of 0% to 15%, (d) mixing said liquid matrix with the dry inorganic perchlorate salt and the dry nitrate salt and thereby making up an initially pourable mixture containing, each in percent by weight, the liquid matrix in an amount of 20% to 50%, the dry inorganic perchlorate salt in an amount of 50% to 80%, and the dry inorganic nitrate salt in an amount of 0% to 22%, and whereby the initially pourable liquid matrix-dry salt mixture is not sensitive to a no.8 blasting cap, (e) pouring the liqid matrix-dry salt mixture into a container, and (f) allowing the liquid matrix-dry salt mixture in the container to cure with formation of a primer which is detonatable using a no.8 blasting cap. With respect to the inventive primer, these objects are also achieved in that the primer is obtainable by the steps (a) to (f) as recited hereinabove. According to the invention, a solid castable explosive product suitable for use as a primer and a small diameter explosive is made up by combining about 20 to about 50% by weight of a liquid matrix and about 50% to about 80% of a dry, insensitive, oxidizer salt or mixture of such oxidizer salts. Preferred salts are inorganic chlorate or perchlorates. The composition of the invention is hereinafter referred to as matrix-dry salt mixture. The inventors discovered that such a mixture cures to a solid if it contains a substantial amount of the dry perchlorate salt or salts. Curing takes place rather quickly, but, before it does, the matrix-dry salt mixture can be pressed, poured, or cast into a mold. The molded product can be detonated by a pentolite detonator of about 8 grams. Embodiments contain amounts of inorganic perchlorates that can be detonated with a No. 8 blasting cap, preferably with a No. 6 blasting cap. A typical liquid matrix includes from about 50% to about 84% by weight of a non-explosive liquid fuel, preferably a polyhydric glycol such as diethylene glycol; 0 to about 22% by weight of an inorganic nitrate oxidizer salt, such as ammonium nitrate, potassium nitrate, sodium nitrate, or calcium nitrate; 0% to about 15% percent by weight water; 0% to about 15% by weight of a water-soluble polymer thickener such as guar gum; 0% to about 5% by weight of an acid such as glacial acetic acid; and 0 to about 2% by weight of a surfactant. The fuel is a water soluble, oxygenated, organic material of low volatility. Examples of the preferred fuel include polyhydric alcohols, such as glycerol, ethylene glycol, diethylene glycol, triethylene glycol, tetraethylene glycol, propylene glycol, dipropylene glycol, tripropylene glycol, and mixtures thereof. Also preferred are still bottoms remaining from the purification of the above, because of their low cost. Depending on their composition, still bottoms can be used alone or in combination with any of the above polyhydric alcohols. As an additional option the matrix can include a cross-linking agent such as potassium pyroantimonate. The final mixture includes about 50 to about 80% by weight of a dry, inorganic perchlorate salt. Sodium perchlorate is preferred but ammonium perchlorate can be used. The final mixture can also include an additional 0% to about 22% by weight of a dry salt such as ammonium nitrate, calcium nitrate, sodium nitrate, potassium nitrate, or mixtures thereof in addition to any nitrate salt that may be included in the matrix. Some or all of this additional dry salt can be sodium chloride. Thus, as the price and availability of the ingredients vary, the primers can be formulated to minimize cost. A rough guide to formulating the primers of this invention is to proportion the inorganic oxidizers and the organic fuels so that all of the hydrogen atoms in the formulations are converted to water and all the oxygen atoms in the formulations are converted to carbon dioxide. However, wide departures from this guide yield primers with good mechanical properties that detonate reliably with a No. 8 blasting cap. Initially, upon mixing the liquid matrix with the dry, inorganic, oxidizer salt or salts, a pourable or pumpable mixture is formed. On standing anywhere from twenty minutes to several hours, depending on the formulation and temperature, the mixture cures to a solid, waxy mass with good mechanical properties. The cure mechanism is not well understood, especially with those formulations in which the water soluble polymer is not deliberately crosslinked, but may involve interactions in which the matrix polyols act as polydentate ligands toward the oxidizer cations. This method of making a solid, castable explosive is a safety improvement over prior art cast primers, especially when sodium perchlorate is employed, because none of the starting materials is self-explosive and it is not necessary to heat the mixture in order to obtain an extrudable, pourable, or pumpable composition. In fact, only a mildly exothermic reaction takes place in making up the liquid matrix. Cooling the matrix before adding the dry product can keep the mixture pourable for a longer period of time, i.e., extend the pour life or pot life. The resulting cast primer is economical, heat resistant, modestly water resistant, and has an explosive strength equivalent to that of prior art cast primers. The use of a hot melt seal on top of the explosive solid in the container renders the container and contents water-tight. Another surprising safety feature of the invention is that the primer tends to increase in detonation sensitivity as it cures, thereby allowing for safer mixing and handling in a less sensitive state. This phenomenon is opposite that of conventional primers or boosters. Another distinct advantage of the primers of the present invention over the prior art is the fact that their performance in terms of shock wave velocity improves as their density increases. The optimum density for certain formulations is 1.80 grams/cc. Surprisingly, formulations show only slightly diminished activity and performance down to 1.50 grams/cc. This is in direct contrast with many primers, which give reduced velocity as the density increases. For example, micro-balloons or air entrapment must be used to lower density in order to make primers from materials such as ANFO emulsions or slurries. Also, the self-explosives usually require blending to give an optimum density of about 1.5 to 1.6 grams/cc. Of course, the objective is to maximize borehole pressure which is a function of both velocity and density. Detailed Description of the Best Mode Contemplated The solid explosive of the invention is made from a mixture of a liquid matrix and a dry oxidizer salt or salts, i.e., a matrix-dry salt mixture. After combining, the matrix-dry salt mixture is transferred to a primer container or mold. The resulting molded mixture cures to a solid product in about two hours, more or less, depending on the temperature, the fluidity of the mixture when made, the particle size and particle size distribution of the dry solid oxidizers, and the amount of dry salt or salts used. If desired, a surfactant may be added to the liquid matrix to slow down the rate of cure. A typical matrix of the invention comprises from about 50% to about 84% by weight of a non-explosive liquid fuel, such as diethylene glycol, other polyhydric glycols, or mixtures thereof; from 0% to about 15% by weight of water; from 0% to about 22% by weight of an organic or inorganic nitrate salt, such as calcium nitrate, ammonium nitrate, or sodium nitrate; from 0 to about 15% of a water soluble polymeric thickener, such as guar gum; from 0% to about 5% by weight of an acid, such as glacial acetic acid; and from 0% to about 2% by weight of a surfactant. The oxidizer salt is an inorganic perchlorate salt, such ammonium perchlorate, sodium perchlorate, or mixtures thereof. A substantial portion of the oxidizer salt must be supplied in a dry form in order to obtain primers with good mechanical properties. The dry oxidizer salt can include lesser amounts of dry nitrate salts. The matrix-dry salt mixture comprises from about 50% to about 80% by weight of a dry inorganic perchlorate, from 0% to about 15% by weight of a dry nitrate salt; and from about 20% to about 50% by weight matrix. In the examples below of matrix-dry salt mixtures, the 68% perchlorate and 32% matrix blend illustrates the greatest tendency to shorter pot life or pour life. The use of 10% sodium nitrate, substituting for perchlorate, extends the pot life in mixes ranging from 10 lb. to 25 lb. (4.5 kg to 11.3 kg), for a matter of 30 seconds to 1.5 minutes. Also, the addition of various surfactants, such as Amphoteric L and Amphoteric C, both avaiable from Exxon Chemical Company, Milton, Wisconsin, in amounts of 0.25% to 0.5% of the final batch weight, increase pot life. However, the final density may be reduced from 0.5 gm/cc to 0.1 gm/cc because of the nature of the surfactants. This pot life extension becomes moot if continuous mixing is employed. It has also been found that particulate size of the sodium perchlorate has an effect on pot life. The following table shows the percent retained in U.S. Standard Sieves for three samples identified as #1, #2, and #3. U.S. Standand Sieve #1 #2 #3 25 --- --- 0.0% 40 --- 0.4% 6.8% 50 20.6% 9.2% 56.4% 70 29.6% 47.8% 88.4% 80 32.3% --- --- 100 35.2% 82.4% 96.0% As indicated only 35.2% of the #1 sample was retained on a 100 mesh sieve. When added to matrix, this sodium perchlorate set up to be not pourable in less than one minute. The #2 and #3 samples had acceptable pour times with 10 lb. to 30 lb. (4.5 kg to 13.6 kg) batches of up to 3 to 4 minutes. With 80% to 90% retained on 100 mesh sieve, pour times have been found to be adequate for batch mixing and pouring. Sodium perchlorate is the preferred salt from a safety standpoint. Ammonium perchlorate is also quite safe to handle but is much more expensive. These salts yield a final product that is much safer to handle than the usual primers. The higher the amount of perchlorate, the greater the density and ease with which the primers are detonated. In a first example of the invention, the matrix had the following formula: Diethylene Glycol 75% Water 10% Calcium Nitrate 12.4% Guar Gum 2.5% Glacial Acetic Acid 0.1% In making up this matrix, the calcium nitrate was first dissolved in water. This solution was added to the non-explosive liquid fuel, i.e., diethylene glycol, wherein a mild exothermic reaction took place. It was desirable to keep the temperature of the matrix low, or to lower it after the exothermic reaction. Keeping the temperature low extended the time in which the freshly made-up matrix-dry salt mixture remained transferable. After the aqueous solution containing the nitrate was added to the non-explosive liquid fuel, guar gum was suspended in an aliquot of the liquid fuel, water, and the nitrate salt. Once suspended it was added to the liquid fuel-water-nitrate mixture. The liquid matrix in such a formulation can include part of the overall amount of sodium perchlorate as an aqueous solution thereof such as is available from commercial sources. Of course, if added to the matrix as a solution, the amount of water used as such is reduced to keep the overall amount of water within an acceptable range. The glacial acetic acid was added next and mixed. Glacial acetic acid is a viscosity enhancer in the guar system. The matrix was now ready to be mixed with the dry salt. The matrix was of low viscosity initially and thickened with time as the guar dissolved. On standing for several hours it became thick and honey-like. However, it has been found that there is no observed change or difference in the handling and performance of the final product whether the matrix is used fresh or aged for several days. Dry sodium perchlorate salt was added to the liquid matrix to make up a matrix-dry salt mixture that was 67% by weight sodium perchlorate and 33% by weight matrix. The sodium perchlorate used in this example and the other examples below was essentially dry, i.e, less than a percent or so water. However, it is believed that since some water is present in all acceptable formulations, it is not necessary that the dry salt be essentially anhydrous and that perhaps even the monohydrate is dry enough to be used to form the fluid liquid matrix-dry salt mixture. It has been discovered in accordance with the invention, that the fluid mixture is not sensitive to a No. 8 blasting cap, while the finished product that hardens after about two hours is sensitive to a No. 8 blasting cap. This greatly adds to the margin of safety in handling the mixture. The final product had a density of 1.49 grams/cc. A one pound (454 gram) charge was detonated on a steel plate of ¾ inch (1.9 centimeter) thickness and blasted a hole in the plate. In a second example, the liquid matrix had the following formula: Aqueous Solution of Sodium Perchlorate (61%) 30% Calcium Nitrate 10% Diethylene Glycol 57% Guar Gum 2.9% Glacial Acetic Acid .1% Dry sodium perchlorate was added to the matrix to make a final product that was 60% dry sodium perchlorate and 40% matrix. The final product had a density of 1.40 grams/cc. A one pound (454 gram) charge was sensitive to a No. 8 blasting cap. The charge was detonated on a ¾ inch (1.9 centimeter) thick steel witness plate and caused spalling of the plate. In a third example, the liquid matrix had the following formula: Aqueous Solution of Sodium Perchlorate (61%) 20% Calcium Nitrate 10% Diethylene Glycol 67% Guar Gum 3% Glacial Acetic Acid .1% Dry sodium perchlorate was added to the matrix to make a final product that was 65% dry sodium perchlorate and 35% matrix. The final product had a density of 1.40 grams/cc. A one pound (454 gram) charge detonated with a No. 8 blasting cap. The charge was detonated on a ¾ inch (1.9 centimeter) thick steel witness plate and caused spalling of the plate. In a fourth example, the liquid matrix had the following formula: Aqueous Solution of Sodium Perchlorate (61%) 35% Calcium Nitrate 10% Diethylene Glycol 53.5% Guar Gum 1.5% Dry sodium perchlorate was added to the matrix to make a final product that was 55% dry sodium perchlorate and 45% matrix. The final product had a density of 1.40 grams/cc. A one pound (454 gram) charge detonated with a No. 8 blasting cap. In a fifth example, the liquid matrix had the following formula: Aqueous Solution of Sodium Perchlorate (61%) 25% Diethylene Glycol 73% Guar Gum 2% Dry sodium perchlorate was added to this matrix to make a final product that was 62% dry sodium perchlorate and 38% matrix. The final product had a density of 1.54 grams/cc. A one pound (454 gram) charge was sensitive to a No. 8 blasting cap. The charge was detonated on a ¾ inch (1.9 centimeter) thick steel witness plate and blasted a hole in the plate. In sixth, seventh, eighth, and ninth examples, the liquid matrix had the following formula: Diethylene Glycol 74% Water 11% Calcium Nitrate 12% Guar Gum 2% Glacial Acetic Acid 1% In the sixth example using the above matrix, dry sodium perchlorate was added to the matrix to make a final product that was 68% dry sodium perchlorate and 32% matrix. A 250 gram charge was sensitive to a No. 8 blasting cap. The charge was detonated on a ¾ inch (1.9 centimeter) thick steel witness plate and blasted a hole in the plate. In the seventh example using the above matrix, dry sodium perchlorate was added to the matrix to make a final product that was 53% dry sodium perchlorate and 32% matrix. The remaining 15% of the final product was made up with additional calcium nitrate. A 250 gram charge was sensitive to a No. 8 blasting cap. In the eighth example using the above matrix, dry sodium perchlorate was added to the matrix to make a final product that was 53% dry sodium perchlorate, 32% matrix. The remaining 15% of the final product was made up with sodium nitrate. A 250 gram charge was sensitive to a No. 8 blasting cap. In the ninth example using the above matrix, dry sodium perchlorate was added to the matrix to make a final product that was 60.5% dry sodium perchlorate and 32% matrix. The remaining 7.5% of the final product was made up with additional sodium nitrate. The final product had a density of 1.72 grams/cc. A one pound (454 gram) charge was sensitive to a No. 8 blasting cap. The charge was detonated on a ¾ inch (1.9 centimeter) thick steel plate and blasted a ½ to ¾ inch (1.27 to 1.9 centimeter) hole in the plate. In a tenth and eleventh example, the liquid matrix had the following formula: Diethylene Glycol 84% Water 12.5% Guar Gum 2.4% Glacial Acetic Acid 1.1% In the tenth example using the above matrix, dry sodium perchlorate was added to the matrix to make a final product that was 64.5% dry sodium perchlorate and 28% matrix. The remaining 7.5% of the final product was made up with calcium nitrate. The final product had a density of 1.67 grams/cc. A one pound (454 gram) charge was sensitive to a No. 8 blasting cap. In the eleventh example using the above matrix, dry sodium perchlorate was added to the matrix to make a final product that was 53% dry sodium perchlorate and 32% matrix. The remaining 15% of the final product was made up with calcium nitrate. The final product had a density of 1.64 grams/cc. A one pound (454 gram) charge was sensitive to a No. 8 blasting cap. In a twelfth example, the matrix had the following formula: Diethylene Glycol 75% Water 11.5% Calcium Nitrate 13.5% In this twelfth example using the above matrix, dry sodium perchlorate was added to the matrix to make a final product that was 58% dry sodium perchlorate and 32% matrix. The remaining 10% was sodium nitrate. The final product had a density of 1.75 to 1.80 grams/cc with good mechanical properties. A one pound (454 gram) charge was sensitive to a No. 8 blasting cap and blasted a hole 1.0 to 1.5 inches (2.54 to 3.81 centimeters) in diameter in a ¾ inch (1.9 centimeter) thick steel witness plate. In a thirteenth example using the above matrix, dry ammonium perchlorate and sodium nitrate was added to the matrix to make a final product that was 58% dry ammonium perchlorate, 10% sodium nitrate, and 32% matrix. The final product had a density of 1.75 to 1.80 grams/cc with good mechanical properties. A one pound (454 gram) charge was sensitive to a No. 8 blasting cap and blasted a hole 1.0 to 1.5 inches (2.54 to 3.81 centimeters) in diameter in a % inch (1.9 centimeter) thick steel witness plate. Similar results were obtained using a final product that was 68% ammonium perchlorate and 32% matrix. Tests on the various examples showed that velocity ranged from 19,000 to 23,000 ft/sec (5,791 meters/sec to 7,010 meters/sec) for the various final products depending on the formulation.

Claims: A method of preparing an explosive product suitable for use as a primer and as a small diameter explosive comprising the following steps: (a) selecting a dry inorganic perchlorate salt from the group consisting of sodium perchlorate, potassium perchlorate, ammonium perchlorate and mixtures thereof, (b) selecting a dry inorganic nitrate salt from the group consisting of ammonium nitrate, calcium nitrate, sodium nitrate, potassium nitrate and mixtures thereof, (c) preparing a liquid matrix containing a water soluble oxygenated organic fuel of low volatility in an amount of 50% to 84% by weight, said water soluble oxygenated organic fuel being selected from the group of polyhydric alcohols consisting of glycerol, ethylene glycol, diethylene glycol, triethylene glycol, tetraethylene glycol, propylene glycol, dipropylene glycol, tripropylene glycol, still bottoms remaining from their purification and mixtures thereof, and optionally further containing, each in percent by weight, a thickener in an amount of 0% to 15%, a nitrate salt in an amount of 0% to 22%, an acid in an amount of 0% to 5%, and water in an amount of 0% to 15%, (d) mixing said liquid matrix with the dry inorganic perchlorate salt and dry nitrate salt and thereby making up an initially pourable mixture containing, each in percent by weight, the liquid matrix in an amount of 20% to 50%, the dry inorganic perchlorate salt in an amount of 50% to 80%, and the optional dry inorganic nitrate salt in an amount of 0% to 22%, and whereby the initially pourable liquid matrix-dry salt mixture is not sensitive to a no.8 blasting cap, (e) pouring the liquid matrix-dry salt mixture into a container, and (f) allowing the matrix-dry salt mixture in the container to cure with formation of an explosive product suitable for use as a primer and as a small diameter explosive which is detonatable using a no. 8 blasting cap. The method according to claim 1, characterized in that the steps a) to f) are carried out at ambient temperature. The method according to claim 2, characterized in that during step d) the liquid matrix-dry salt mixture exhibits an exotherm upon mixing. The method according to any one of claims 1 to 3, characterized in that the dry inorganic perchlorate is dry sodium perchlorate. The method according to claim 4, characterized in that part of the selected dry inorganic perchlorate is added as an aqueous solution to the liquid matrix in step d). The method according to any one of claims 1 to 5, characterized in that the nitrate salt is calcium nitrate. The method according to any one of claims 1 to 6, characterized in that the polyhydric alcohol is diethylene glycol. The method according to any one of claims 1 to 7, characterized in that the thickener is guar gum. The method according to any one of claims 1 to 8, characterized in that the acid is glacial acetic acid. The method according to claim any one of claims 1 to 9, characterized in that a cross-linking agent is added in step c). The method according to claim 10, characterized in that the cross-linking agent is potassium-pyroantimonate. The method according to any one of claims 1 to 11, characterized in that an inert chloride salt is added in step d). A solid, cured explosive product in a container for use as a primer and a small diameter explosive which is detonatable using a no. 8 blasting cap obtainable by the method according to any one of claims 1 to 12.

Inventors: STROMQUIST DONALD M, WATHEN BOYD J, STROMQUIST, DONALD M., WATHEN, BOYD J.
Applicants: DYNO NOBEL INC, DYNO NOBEL INC.
Application year: 1992
Main classification: C06B47
IPC codes: C06B45, C06C7, C06B47, C06B21, C06B31