US3222232A - Aqueous explosive slurries containing sulfur compounds having a low coefficient of expansion - Google Patents

Aqueous explosive slurries containing sulfur compounds having a low coefficient of expansion Download PDF

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US3222232A
US3222232A US350550A US35055064A US3222232A US 3222232 A US3222232 A US 3222232A US 350550 A US350550 A US 350550A US 35055064 A US35055064 A US 35055064A US 3222232 A US3222232 A US 3222232A
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explosive
expansion
sodium
nitrate
slurry
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William L Schwoyer
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Trojan Powder Co
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    • CCHEMISTRY; METALLURGY
    • C06EXPLOSIVES; MATCHES
    • C06BEXPLOSIVES OR THERMIC COMPOSITIONS; MANUFACTURE THEREOF; USE OF SINGLE SUBSTANCES AS EXPLOSIVES
    • C06B47/00Compositions in which the components are separately stored until the moment of burning or explosion, e.g. "Sprengel"-type explosives; Suspensions of solid component in a normally non-explosive liquid phase, including a thickened aqueous phase
    • C06B47/14Compositions in which the components are separately stored until the moment of burning or explosion, e.g. "Sprengel"-type explosives; Suspensions of solid component in a normally non-explosive liquid phase, including a thickened aqueous phase comprising a solid component and an aqueous phase

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  • Explosive slurries containing appreciable quantities of water or other fluids have recently become of considerable interest in the explosive art. These mixtures have a greater versatility than dry mixtures, because they can be used under conditions where water cannot be excluded.
  • the fluid content of the slurries is more than that which is absorbed by the components of the mixture, and is sufficient to act at least in part as a suspending agent for the explosive ingredients. Such a fluid content in most cases ranges from about 0.5% to more than depending upon the materials present in the mixture, and upon the consistency desired.
  • a slurry having a reasonably stiff consistency, containing as little as 10% fluid, may be preferred for use in bulk in wet bore holes Where the composition may be diluted with fluids such as water already present. Thickening or gelling agents are employed when thick slurries are required containing high proportions of fluids. A slurry that can be poured may be desired for use in bulk in dry bore holes, and such a slurry is easily obtained by using a rather large proportion of fluid, for example, 20 to 50%, without a thickening or gelatinizing agent.
  • the slurries upon being subjected to relatively hot day temperatures, the slurries will expand, but when the temperature decreases, as at nightfall or during normal climatic changes, the explosive compositions do not return to their original size, but to a size short of that.
  • the explosive composition contained within the cartridge continuously exerts an undue pressure on the plastic container which is suflicient in time to cause rupture. Rupture is, of course, undesirable whenever it occurs.
  • explosive slurries based on inorganic nitrates, aluminum and water can be so formulated as to have a low coeflicient of expansion with temperature, by incorporating therein a small amount of a thiosulfate or organic sulfonate.
  • a thiosulfate or organic sulfonate not only do the compositions of the invention display a markedly reduced tendency to expand on heating, but if they expand, they return to approximately their original normal dimensions when the temperature is again lowered. Thus, they display essentially no irreversible expansion characteristics.
  • the explosive slurries of this invention are therefore more readily stored under a wide range of temperatures, and hence are safer to handle and use over such temperatures.
  • the thiosulfates M S O which can be employed can be represented by the following formula:
  • Min ⁇ Z s 0 M is a cation and m and n are integers taken to satisfy the valences of M and the thiosulfate anion S' O
  • Exemplary are the sodium, potassium, lithium, ammonium, calcium, barium and magnesium thiosulfates, which may be either in the anhydrous form or in the form of the respective hydrates.
  • the organic hydrocarbon sulfonates which can be employed have the general formula RSO' M, where M is a cation, such as alkali metal, such as sodium and potassium, ammonium, an alkaline earth metal, such as calcium or magnesium, or an organic amine such as triethanolamine, and R is an organic hydrocarbon group, such as an alkyl, aryl, arylalkyl, alkylaryl or cycloalkyl group containing from about three to about fifty carbon atoms.
  • Such hydrocarbon groups can also be substituted with carbonyl groups, ester groups, ether groups, sulfide groups, sulfuryl groups and additional sulfonate groups.
  • Typical are the sodium petroleum hydrocarbon sulfonates, and the sodium benzene sulfonates, such as sodium benzene sulfonates, sodium dodecyl benzene sulfonate and sodium keryl benzene sulfonate.
  • the benzene sulfonates have the structural formula:
  • M is a cation and R is hydrogen or an alkyl group of from one to thirty carbon atoms.
  • a preferred class of hydrocarbon sulfonates are the ester-substituted sulfonates. Such compounds have the structural formulas:
  • R R and R are hydrocarbon groups containing from about one to about fifty carbon atoms.
  • R and R can for example each be alkyl, aryl, alkylaryl, arylalkyl or cycloalkyl, and R can be a bivalent alkylene, arylene, alkylarylene, arylalkylene or cycloalkylene group.
  • R is a bivalent alkylene group and contains from about two to ten carbon atoms, and R and R are alkyl groups containing from about five to about twenty carbon atoms.
  • thiosulfate or sulfonate will be made wit-h regard to the fluid or fluid mixture used as a vehicle for the slurry. It should be soluble or easily dispersible in the vehicle. If only certain compounds are available, their solubility characteristics may determine the nature of the vehicle. Thus, water or aqueous vehicles are usually required for the thiosulfates.
  • the organic sulfonates can be used with water, oil, or mixtures thereof.
  • the oxidizing agent employed in the explosive slurry of this invention should be an inorganic nitrate.
  • Ammonium nitrate and nitrates of the alkali and alkaline earth metals such as sodium nitrate, potassium nitrate, calcium nitrate, magnesium nitrate, strontium nitrate and barium nitrate, are exemplary inorganic nitrates. Mixtures of several nitrates such as, for example, mixtures of sodium and ammonium nitrates, also yield excellent results.
  • the inorganic nitrates may be fine, coarse, or a blend of line and coarse materials. Mill and prill inorganic nitrates are quite satisfactory. For best results, the inorganic nitrates are usually fine grained.
  • nitrate oxidizers there is generally employed one or more fuels, including metal fuels and carbonaceous fuels, and an amount of water or water and oil sufficient to give the mixture the consistency desired, be it the consistency of a semi-solid material or the consistency of a free-flowing slurry.
  • fuels including metal fuels and carbonaceous fuels
  • water or water and oil sufficient to give the mixture the consistency desired, be it the consistency of a semi-solid material or the consistency of a free-flowing slurry.
  • a sensitizing explosive can also be included, as an optional component.
  • the preferred sensitizing explosive is nitrostarch, but any sensitizing explosive known to the art can be used, alone or in admixture.
  • Known sensitizing explosives which are useful include, for example, trinitrotoluene, dinitrotoluene, pentaerythritol tetranitrate, nitrostarch, trimethylolethene trinitrate, pentolite (a mixture of equal parts by weight of pentaerythritol tetranitrate and trinitrotoluene), cyclonite (RDX, cyclotrimethylene trinitramine), nitrocellulose, Composition B (a mixture of up to 60% RDX, up to 40% TNT and 1 to 4% wax), Cyclotol (Composition B without the wax), tetryl, and smokeless powder such as carbine ball powder.
  • the amount of thiosulfate or sulfonate required for a low coefiicient of expansion in accordance with this invention is small. Generally, from 1 to 3% is employed for optimum results, although amounts as low as 0.3% give a reduction in the coefiicient of expansion. More than about 3% would not usually be employed, as such large amounts are unnecessary to achieve the desired result, and therefore wasteful.
  • nitrate oxidizer and of sensitizing explosive if used, will depend upon the sensitivity and explosive shock wave desired and these, again, are dependent upon the particular nitrate and sensitizing explosive.
  • the proportions are not critical in any way.
  • the nitrate oxidizer is used in an amount within the range from about 10 to about 95%
  • the sensitizing explosive can be used in an amount within the range from to about 40% by weight of the explosive composition. From about 25 to about 30% sensitizing explosive and from about 50 to about 70% nitrate oxidizer give the best results.
  • sensitizing explosives of any particle size can be used. They can, for example, be fine, coarse, or a blend of fine and coarse material. Some materials, such as nitrostarch, are commercially available as very finely-divided powders, and so also is trinitrotoluene. Such available materials are employed to advantage, because in most cases they tend to produce compositions having a greater explosive effect.
  • the explosive compositions of the invention include aluminum, preferably in particulate form, for example aluminum powder, atomized aluminum, granular aluminum, or flake aluminum, which also serves as a lubricity-improving agent.
  • Aluminum can be used in the form of alloys such as aluminum-magnesium alloys.
  • Other metal fuels can also be used in conjunction with the aluminum, such as, for example, magnesium and ferrosilicon.
  • the metal fuel will usually comprise from about 0.5% to about 20% and preferably from 0.5 to 15% of the composition, of which fuel at least 50% is aluminum. If the amount of aluminum exceeds 15%, best stabilization is obtained if the aluminum is coarse, i.e., if at least 50% of the particles are 60 mesh or larger.
  • a carbonaceous fuel can be included, such as powdered coal, petroleum oil, coke dust, charcoal, bagasse, dextrine, starch, wood meal, flour bran, pecan meal, and similar nut shell meals.
  • a carbonaceous fuel when present will comprise from about 0.5 to about 30% of the mixture. Mixtures of metal and carbonaceous fuels can be used, if desired.
  • An antacid, or other stabilizing material such as zinc oxide, calcium carbonate, aluminum oxide, and sodium carbonate, can also be added.
  • Such ingredients will comprise from about 0.3 to about 2% of the mixture.
  • the amount of water and other fluid employed in the composition will vary with the consistency desired of the final mixture. Generally, when a semi-solid mixture is desired, especially for use in preparing cartridges, as little as 0.5% of water or mixture of water and other fluid such as oil can be used, and generally not more than 10% is needed. Where free-flowing slurries are desired, larger amounts of water or aqueous mixtures are generally employed, in most cases within the range of from about 10 to about 40%, although in some cases as much as 50% of fluid can be used.
  • This slurry can be decreased to meet any need by incorporating a thickening or gelatinizing agent.
  • a thickening or gelatinizing agent should be soluble or dispersible in the dispersing fluid and inert to the other ingredients present.
  • the thickened slurry can be used to form explosive cartridges in the same manner as the slurries normally having a semi-solid consistency.
  • An oil slurry can be thickened by any of the noncarbonaceous inorganic oil thickeners useful in making thickened oils and greases, such as finely divided silica, available under the trade names Cab-O-Sil and Ludox, and silica aerogels, for example Santocel ARD and Santocel C, and like inorganic gelling agents, such as alumina, attapulgite and bentonite, can be used.
  • silica aerogels for example Santocel ARD and Santocel C, and like inorganic gelling agents, such as alumina, attapulgite and bentonite, can be used.
  • Other oil-gelling agents are disclosed in US. Patents Nos. 2,655,476 and 2,711,393. These are well known materials, and any of these known to the art can be used. The amount of such thickening agent will depend on the consistency desired, and usually will be within the range from 0 up to about 5%.
  • Enough thickener can be added to gel the oil, and water-proofing agents such as are disclosed in US. Patents Nos. 2,554,222,, 2,655,476 and 2,711,393 also can be incorporated as well to impart water resistance to the gelled oil slurry.
  • An aqueous slurry can be thickened by any watersoluble or water-dispersible thickener, such as, for example, carboxymethyl cellulose, methyl cellulose, guar gum, psyllium seed mucilage, and pregelatinized starches such as Hydroseal 3B.
  • the amount of such thickening 5 agent will depend on the consistency desired, and usually will be Within the range from to about
  • the explosive of the invention can, if desired, be fired with the aid of a booster charge. Any conventional cap-sensitive booster charge available in the art can be employed. Pentaerythritol tetranitrate, Composition B and pentolite are exemplary.
  • the booster charge preferably is non-shock or impact sensitive. The amount of booster charge required depends, of course, upon the amount and sensitivity of the explosive mixture.
  • the explosive mixture is readily prepared by simple mixing of the ingredients.
  • the solid materials including the thiosulfate or sulfonate, the inorganic nitrates and sensitizing explosives, if any, fuels, and antacid, if any, would usually be mixed at first, to form a homogeneous blend, and the slurrying liquid and slurry liquid thickener, if required, would be added with stirring to bring the mixture to the desired consistency.
  • the consistency is usually comparable to that of a gelled oil or thick, barely pourable mixture, and the mixture is filled or extruded into open-ended containers, using conventional filling or extrusion equipment, to produce the explosive package.
  • the containers can be formed of any container material not dissolved or attacked by the slurry liquid or liquids.
  • Heavy plastic is inexpensive and available in sufficient thickness of wall, and is therefore preferred.
  • Typical plastic and cellulosic materials which can be used include polyethylene, ethyl cellulose, cellulose acetate, polypropylene, polytetrafiuoroethylene, nylon, polyvinyl chloride, polystyrene and polyvinylidene chloride, and nonferrous metals, such as tin, copper and aluminum.
  • Fibrous materials such as Wood, paper, and cardboard can be used, if waterproofed or otherwise made resistant to the slurrying liquid.
  • EXAMPLE 1 An explosive mixture of semi-solid consistency (A in the table below) was prepared using nitrostarch, fine water and then added to the mixture. The proportions of the final explosive compositions were as follows:
  • Composition A was quite stilt, and was easily extruded through conventional extrusion nozzles into cartridges 36 inches long by 1% inches in diameter made of string wrapped paper encased in polyethylene, 2 to 3 mils in thickness.
  • a 4 gram cast pentolite booster containing a No. 6 blasting cap was inserted into the cartridge. The cartridge was then inserted in a bore hole 2% inches in diameter. The cartridge was fired, and gave a detonation rate greater than 5000 meters per second, indicating that the composition was a satisfactory explosive.
  • each cycle included heating the cartridges at to 125 F. for 7 to 7% hours, approximately equal to the time they might be subjected to that temperature under conditions of use, and then lowering the temperature to 66 to 68 F. After each cycle three diameter measurements were taken, at marked places on each cartridge, at both end and the center and the measurements were averaged, and reported as the average diameter of the cartridge at each cycle.
  • test included a series of control cartridges prepared in the same manner except that the control explosive composition (B) did not contain sodium thiosulfate.
  • Cartridges Nos. 1 to 6 which were filled with explosive compositions containing sodium thiosulfate in accordance with this invention, showed a total increase in diameter over the entire treating period ranging from Five of the cartridges containing '7 8 the explosive composition of this invention showed a Percent percent increase in diameter of less than 0.8% over the Guar gum 1.00 entire cycle.
  • none of the cartridges con- Sodium carboxymethyl cellulose 0.60 taining the explosive compositions of this invention had Zinc oxide 1.00 expanded sufiiciently during the test to cause the rupture Water 9.25 of the polyethylene cartridge.
  • compositions were prepared to show that the that had the four ruptured cartridges been able to sursulfur containing compound of this invention actually make the temperatures, their percent increase in diameter exerts its stabilizing action upon the nitrate and the aluwould have exceeded the 6.4% withstood by composition minum components of the explosive slurry.
  • the two No. 8. compositions each contained 85 parts of sodium nitrate,
  • the object of this experiment tridges containing Composition A were subjected to a was to determine the time necessary for the cork to be more rigorous test.
  • the cartridges forced out of the test tube because of the expansion of were first held at a temperature of 70 F. for 24 hours the nitrate-aluminum slurry. It was found that the comand the diameters measured.
  • the temperature was then position which did not contain sodium thiosulfate exraised to 105 F., maintained for 24 hours, and therepanded sufiiciently so as to force the cork out of the after cooled to 72 F. for 24 hours.
  • the temperature test tube 24 minutes after immersion in the water bath.
  • EXAMPLE 4 1.00 baths at 98 C. in order to determine the length of time *After this time, test was stopped without the cork having been forced from the tube.
  • This example shows that sodium thiosulfate and the dioctyl ester of sodium sulfosuccinic acid substantially inhibited thermal expansion of the composition.
  • the coeificient of expansion of sodium nitrate varies with impurities in the batch, and this accounts for the fact that the composition in Example 3 forced the cork from the tube in 24 minutes, while the composition of the example required 85 minutes.
  • compositions A and B were substantially identical in explosive properties, but Composition B was found to have negligible coeflicient of expansion, as compared to Composition A without sodium thiosulfate.
  • Composition B was as good an explosive as the thiosulfate-free material A, but had a very low coeificient of expansion.
  • EXAMPLE 9 An explosive mixture of semi-solid consistency (A in the table below) was prepared using nitrostarch, grained mill ammonium nitrate, mill sodium nitrate, flake aluminum, sodium benzene sulfonate, water and the additional ingredients noted in the table below. The nitrostarch, oil and mixed nitrates were thoroughly blended and were then added to the zinc oxide, flake aluminum, guar gum and sodium carboxymethyl cellulose. The sodium benzene sulfonate was dissolved in the water and then added to the mixture. The proportions compositions were as follows:
  • An aqueous slurried explosive in accordance with claim 1 containing sufficient water to impart to the composition a semi-solid consistency.
  • An aqueous slurried explosive in accordance with claim 1 comprising a thickening agent in an amount to increase the consistency of the composition.
  • An aqueous slurried explosive in accordance with claim 1 comprising an explosive sensitizer.
  • a method of reducing the coefiicient of thermal expansion of aqueous slurried explosive compositions comprising an inorganic nitrate oxidizer in an amount within the range from about 10 to about particulate aluminum in an amount within the range from about 0.5 to about 20%, and an aqueous liquid in an amount to form a slurry, which comprises incorporating therein a sulfur compound selected from the group consisting of inorganic thiosulfates and organic sulfonates in an amount sufiicient to inhibit thermal expansion.

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Description

United States Patent 3,222,232 AQUEOUS EXPLOSIVE SLURRIES CONTAINING SULFUR CQMPQUNDS HAVING A LOW C0? EFFKCIENT 0F EXPANSION William L. Schwoyer, Allentown, Pa., assignor to Trojan Powder Company, Allentown, Pa., a corporation of New York No Drawing. Filed Mar. 9, 1964, Ser. No. 350,550 Claims. (Cl. 149-43) This invention relates to aqueous explosive slurries resistant to expansion upon exposure to elevated temperatures due to an unusually low coeflicient of expansion with temperature.
Explosive slurries containing appreciable quantities of water or other fluids have recently become of considerable interest in the explosive art. These mixtures have a greater versatility than dry mixtures, because they can be used under conditions where water cannot be excluded. The fluid content of the slurries is more than that which is absorbed by the components of the mixture, and is sufficient to act at least in part as a suspending agent for the explosive ingredients. Such a fluid content in most cases ranges from about 0.5% to more than depending upon the materials present in the mixture, and upon the consistency desired.
A slurry having a reasonably stiff consistency, containing as little as 10% fluid, may be preferred for use in bulk in wet bore holes Where the composition may be diluted with fluids such as water already present. Thickening or gelling agents are employed when thick slurries are required containing high proportions of fluids. A slurry that can be poured may be desired for use in bulk in dry bore holes, and such a slurry is easily obtained by using a rather large proportion of fluid, for example, 20 to 50%, without a thickening or gelatinizing agent.
Such slurries, however, present a packaging problem not encountered with dry mixtures, because, due to their liquid content, they have a high coefiicient of expansion with temperature. This expansion creates special difficulties when explosive slurries are packaged in flexible plastic containers, since the explosive slurry must fill the entire plastic container so that air is excluded therefrom, leaving no air space for expansion. This means that the container must either expand and contract with the slurried contents, or rupture. Even if it expands, dimensions change, usually unevenly, with the result that the container may become oversized for a particular bore hole, and wedge at a bend in the bore hole, if it even fits the hole.
Expansion and contraction within the resiliency limits of the plastic cartridge can be tolerated, and by selecting an appropriate type, grade and thickness of plastic material, the relative expansion coefficients can even be matched. However, some explosive mixtures, particularly those employing an inorganic nitrate as an oxidizer and a metal such as aluminum as a fuel, have an unusually high expansion coeflicient, and require either thick containers, to prevent rupture, or very thin containers which have a high coeflicient of expansion. Neither alternative is very desirable. In addition, such explosive slurries have a tendency to expand irreversibly. That is, upon being subjected to relatively hot day temperatures, the slurries will expand, but when the temperature decreases, as at nightfall or during normal climatic changes, the explosive compositions do not return to their original size, but to a size short of that. As a result, the explosive composition contained within the cartridge continuously exerts an undue pressure on the plastic container which is suflicient in time to cause rupture. Rupture is, of course, undesirable whenever it occurs.
While it is believed that the high expansion coeflicient 3,222,232 Patented Dec. 7, 1955 may be due, in some small part at least, to phase changes or changes in hydration of the inorganic nitrate, it appears that only when aluminum is present does the volume change assume large and undesirable proportions.
It has now been found, in accordance with the invention, that explosive slurries based on inorganic nitrates, aluminum and water can be so formulated as to have a low coeflicient of expansion with temperature, by incorporating therein a small amount of a thiosulfate or organic sulfonate. Not only do the compositions of the invention display a markedly reduced tendency to expand on heating, but if they expand, they return to approximately their original normal dimensions when the temperature is again lowered. Thus, they display essentially no irreversible expansion characteristics. The explosive slurries of this invention are therefore more readily stored under a wide range of temperatures, and hence are safer to handle and use over such temperatures.
The thiosulfates M S O which can be employed can be represented by the following formula:
0 0 Min \Z s 0 M is a cation and m and n are integers taken to satisfy the valences of M and the thiosulfate anion S' O Exemplary are the sodium, potassium, lithium, ammonium, calcium, barium and magnesium thiosulfates, which may be either in the anhydrous form or in the form of the respective hydrates.
The organic hydrocarbon sulfonates which can be employed have the general formula RSO' M, where M is a cation, such as alkali metal, such as sodium and potassium, ammonium, an alkaline earth metal, such as calcium or magnesium, or an organic amine such as triethanolamine, and R is an organic hydrocarbon group, such as an alkyl, aryl, arylalkyl, alkylaryl or cycloalkyl group containing from about three to about fifty carbon atoms. Such hydrocarbon groups can also be substituted with carbonyl groups, ester groups, ether groups, sulfide groups, sulfuryl groups and additional sulfonate groups. Typical are the sodium petroleum hydrocarbon sulfonates, and the sodium benzene sulfonates, such as sodium benzene sulfonates, sodium dodecyl benzene sulfonate and sodium keryl benzene sulfonate. The benzene sulfonates have the structural formula:
SOzM
where M is a cation and R is hydrogen or an alkyl group of from one to thirty carbon atoms.
A preferred class of hydrocarbon sulfonates are the ester-substituted sulfonates. Such compounds have the structural formulas:
wherein M is a cation as above and R R and R are hydrocarbon groups containing from about one to about fifty carbon atoms. R and R can for example each be alkyl, aryl, alkylaryl, arylalkyl or cycloalkyl, and R can be a bivalent alkylene, arylene, alkylarylene, arylalkylene or cycloalkylene group. Preferably, R is a bivalent alkylene group and contains from about two to ten carbon atoms, and R and R are alkyl groups containing from about five to about twenty carbon atoms.
The choice of thiosulfate or sulfonate will be made wit-h regard to the fluid or fluid mixture used as a vehicle for the slurry. It should be soluble or easily dispersible in the vehicle. If only certain compounds are available, their solubility characteristics may determine the nature of the vehicle. Thus, water or aqueous vehicles are usually required for the thiosulfates. The organic sulfonates, on the other hand, can be used with water, oil, or mixtures thereof.
The oxidizing agent employed in the explosive slurry of this invention should be an inorganic nitrate. Ammonium nitrate and nitrates of the alkali and alkaline earth metals, such as sodium nitrate, potassium nitrate, calcium nitrate, magnesium nitrate, strontium nitrate and barium nitrate, are exemplary inorganic nitrates. Mixtures of several nitrates such as, for example, mixtures of sodium and ammonium nitrates, also yield excellent results. The inorganic nitrates may be fine, coarse, or a blend of line and coarse materials. Mill and prill inorganic nitrates are quite satisfactory. For best results, the inorganic nitrates are usually fine grained.
In addition to the nitrate oxidizers, there is generally employed one or more fuels, including metal fuels and carbonaceous fuels, and an amount of water or water and oil sufficient to give the mixture the consistency desired, be it the consistency of a semi-solid material or the consistency of a free-flowing slurry. A sensitizing explosive can also be included, as an optional component.
The preferred sensitizing explosive is nitrostarch, but any sensitizing explosive known to the art can be used, alone or in admixture. Known sensitizing explosives which are useful include, for example, trinitrotoluene, dinitrotoluene, pentaerythritol tetranitrate, nitrostarch, trimethylolethene trinitrate, pentolite (a mixture of equal parts by weight of pentaerythritol tetranitrate and trinitrotoluene), cyclonite (RDX, cyclotrimethylene trinitramine), nitrocellulose, Composition B (a mixture of up to 60% RDX, up to 40% TNT and 1 to 4% wax), Cyclotol (Composition B without the wax), tetryl, and smokeless powder such as carbine ball powder.
The amount of thiosulfate or sulfonate required for a low coefiicient of expansion in accordance with this invention is small. Generally, from 1 to 3% is employed for optimum results, although amounts as low as 0.3% give a reduction in the coefiicient of expansion. More than about 3% would not usually be employed, as such large amounts are unnecessary to achieve the desired result, and therefore wasteful.
The relative proportions of nitrate oxidizer, and of sensitizing explosive if used, will depend upon the sensitivity and explosive shock wave desired and these, again, are dependent upon the particular nitrate and sensitizing explosive. The proportions are not critical in any way. For optimum effect, the nitrate oxidizer is used in an amount within the range from about 10 to about 95%, and the sensitizing explosive can be used in an amount within the range from to about 40% by weight of the explosive composition. From about 25 to about 30% sensitizing explosive and from about 50 to about 70% nitrate oxidizer give the best results.
When the amount of sensitizing explosive is in the lower part of the range, or zero, a large booster is needed. At amounts beyond 40%, the sensitizing effect falls off, and is no longer proportional to the amount of sensitizing explosive added, and therefore amounts beyond 40% are not usually used.
sensitizing explosives of any particle size can be used. They can, for example, be fine, coarse, or a blend of fine and coarse material. Some materials, such as nitrostarch, are commercially available as very finely-divided powders, and so also is trinitrotoluene. Such available materials are employed to advantage, because in most cases they tend to produce compositions having a greater explosive effect.
In addition to these materials, as has been indicated,
the explosive compositions of the invention include aluminum, preferably in particulate form, for example aluminum powder, atomized aluminum, granular aluminum, or flake aluminum, which also serves as a lubricity-improving agent. Aluminum can be used in the form of alloys such as aluminum-magnesium alloys. Other metal fuels can also be used in conjunction with the aluminum, such as, for example, magnesium and ferrosilicon.
The metal fuel will usually comprise from about 0.5% to about 20% and preferably from 0.5 to 15% of the composition, of which fuel at least 50% is aluminum. If the amount of aluminum exceeds 15%, best stabilization is obtained if the aluminum is coarse, i.e., if at least 50% of the particles are 60 mesh or larger.
In addition to the metal fuel, a carbonaceous fuel can be included, such as powdered coal, petroleum oil, coke dust, charcoal, bagasse, dextrine, starch, wood meal, flour bran, pecan meal, and similar nut shell meals. A carbonaceous fuel when present will comprise from about 0.5 to about 30% of the mixture. Mixtures of metal and carbonaceous fuels can be used, if desired.
An antacid, or other stabilizing material, such as zinc oxide, calcium carbonate, aluminum oxide, and sodium carbonate, can also be added. Such ingredients will comprise from about 0.3 to about 2% of the mixture.
The amount of water and other fluid employed in the composition will vary with the consistency desired of the final mixture. Generally, when a semi-solid mixture is desired, especially for use in preparing cartridges, as little as 0.5% of water or mixture of water and other fluid such as oil can be used, and generally not more than 10% is needed. Where free-flowing slurries are desired, larger amounts of water or aqueous mixtures are generally employed, in most cases within the range of from about 10 to about 40%, although in some cases as much as 50% of fluid can be used.
In the case of oil, of course, the viscosity of the oil is a factor to be taken into consideration in determining the amount of fluid added. When mixtures of oil and water are used, there would generally be employed from 2 to 10% Water and from 10 to 30% oil, to give a slurry having a satisfactory fluidity.
The consistency of this slurry, particularly of a freeflowing slurry, can be decreased to meet any need by incorporating a thickening or gelatinizing agent. In this way, it is possible to prepare a thick slurry containing a large proportion of fluid for use in bulk in dry bore holes. The thickening agent should be soluble or dispersible in the dispersing fluid and inert to the other ingredients present. The thickened slurry can be used to form explosive cartridges in the same manner as the slurries normally having a semi-solid consistency.
An oil slurry can be thickened by any of the noncarbonaceous inorganic oil thickeners useful in making thickened oils and greases, such as finely divided silica, available under the trade names Cab-O-Sil and Ludox, and silica aerogels, for example Santocel ARD and Santocel C, and like inorganic gelling agents, such as alumina, attapulgite and bentonite, can be used. Other oil-gelling agents are disclosed in US. Patents Nos. 2,655,476 and 2,711,393. These are well known materials, and any of these known to the art can be used. The amount of such thickening agent will depend on the consistency desired, and usually will be within the range from 0 up to about 5%. Enough thickener can be added to gel the oil, and water-proofing agents such as are disclosed in US. Patents Nos. 2,554,222,, 2,655,476 and 2,711,393 also can be incorporated as well to impart water resistance to the gelled oil slurry.
An aqueous slurry can be thickened by any watersoluble or water-dispersible thickener, such as, for example, carboxymethyl cellulose, methyl cellulose, guar gum, psyllium seed mucilage, and pregelatinized starches such as Hydroseal 3B. The amount of such thickening 5 agent will depend on the consistency desired, and usually will be Within the range from to about The explosive of the invention can, if desired, be fired with the aid of a booster charge. Any conventional cap-sensitive booster charge available in the art can be employed. Pentaerythritol tetranitrate, Composition B and pentolite are exemplary. The booster charge preferably is non-shock or impact sensitive. The amount of booster charge required depends, of course, upon the amount and sensitivity of the explosive mixture.
The explosive mixture is readily prepared by simple mixing of the ingredients. The solid materials, including the thiosulfate or sulfonate, the inorganic nitrates and sensitizing explosives, if any, fuels, and antacid, if any, would usually be mixed at first, to form a homogeneous blend, and the slurrying liquid and slurry liquid thickener, if required, would be added with stirring to bring the mixture to the desired consistency. Where cartridges are to be formed, the consistency is usually comparable to that of a gelled oil or thick, barely pourable mixture, and the mixture is filled or extruded into open-ended containers, using conventional filling or extrusion equipment, to produce the explosive package.
The containers can be formed of any container material not dissolved or attacked by the slurry liquid or liquids. Heavy plastic is inexpensive and available in sufficient thickness of wall, and is therefore preferred. Typical plastic and cellulosic materials which can be used include polyethylene, ethyl cellulose, cellulose acetate, polypropylene, polytetrafiuoroethylene, nylon, polyvinyl chloride, polystyrene and polyvinylidene chloride, and nonferrous metals, such as tin, copper and aluminum. Fibrous materials such as Wood, paper, and cardboard can be used, if waterproofed or otherwise made resistant to the slurrying liquid.
The following examples in the opinion of the inventor represent the preferred embodiments of this invention:
EXAMPLE 1 An explosive mixture of semi-solid consistency (A in the table below) was prepared using nitrostarch, fine water and then added to the mixture. The proportions of the final explosive compositions were as follows:
Composition A was quite stilt, and was easily extruded through conventional extrusion nozzles into cartridges 36 inches long by 1% inches in diameter made of string wrapped paper encased in polyethylene, 2 to 3 mils in thickness. A 4 gram cast pentolite booster containing a No. 6 blasting cap was inserted into the cartridge. The cartridge was then inserted in a bore hole 2% inches in diameter. The cartridge was fired, and gave a detonation rate greater than 5000 meters per second, indicating that the composition was a satisfactory explosive.
Six of the cartridges so prepared were then subjected to expansion tests in four cycles. Each cycle included heating the cartridges at to 125 F. for 7 to 7% hours, approximately equal to the time they might be subjected to that temperature under conditions of use, and then lowering the temperature to 66 to 68 F. After each cycle three diameter measurements were taken, at marked places on each cartridge, at both end and the center and the measurements were averaged, and reported as the average diameter of the cartridge at each cycle.
The test included a series of control cartridges prepared in the same manner except that the control explosive composition (B) did not contain sodium thiosulfate.
The results are recorded below in Table I. The difference between the initial diameter and the diameter after each of the cycles represents the irreversible expansion that has been acquired by the explosive composition. A burst cartridge is indicated by Table I AVERAGE DIAMETER IN INCHES AFTER HEATING AT TEMPERATURE AND TIME INDICATED Cartridge 7 hrs. at 100 7% hrs. at 7 hrs. at 7 hrs. at Increase in diameter No. No. with Initial, 66 F., cooled to 110 F., F., cooled to F., cooled to F. 66 F. cooled to 66 F. 68 F.
68 F. Total Percent Control (no thiosulfate) *The polyethylene cartridge burst at one end during the heating portion of the cycle, the explosive composition escaping therefrom.
The results of Table I show the exceptionally low co- 70 efficient of expansion of the compositions of this in- The sodium thiosulfate was dissolved in the 75 only 0.23% to 1.5%.
vention. Cartridges Nos. 1 to 6, which were filled with explosive compositions containing sodium thiosulfate in accordance with this invention, showed a total increase in diameter over the entire treating period ranging from Five of the cartridges containing '7 8 the explosive composition of this invention showed a Percent percent increase in diameter of less than 0.8% over the Guar gum 1.00 entire cycle. In addition, none of the cartridges con- Sodium carboxymethyl cellulose 0.60 taining the explosive compositions of this invention had Zinc oxide 1.00 expanded sufiiciently during the test to cause the rupture Water 9.25 of the polyethylene cartridge.
In contrast, four out of the seven cartridges which T1118 P Was bumped loadefl Into y contained the control composition, the same composition test tubes, which were stoppered, leaving no air space, as in Cartridges Nos. 1 to 6, except for the absence of and Stored at a temperature between 100 and 130 F. sodium thiosulfate, were unable to withstand the test 10 r fi months N expanslorg sufficient to w ff the conditions, and ruptured as a result of the expansion e tube pp Was noted, 1I 1d1at1ng f l I10 pp of the explosive composition beyond the elastic limit of (liable 61413211181011 0f the exploslve composltlon had the polyethylene container during the course of the heat- Cuffeding cycles. Of the three control compositions which survived the test conditions, No. 8 showed an increase 5 AMPLE 3 in diameter of 6.4% and Nos. 12 and- 13 showed increases of 3.3% and 4.4% respectively. It can only be assumed Two compositions were prepared to show that the that had the four ruptured cartridges been able to sursulfur containing compound of this invention actually vive the temperatures, their percent increase in diameter exerts its stabilizing action upon the nitrate and the aluwould have exceeded the 6.4% withstood by composition minum components of the explosive slurry. The two No. 8. compositions each contained 85 parts of sodium nitrate,
Thus, it can be seen that the presence of a small 12 parts of flake aluminum and 3 parts of water. Two quantity of sodium thiosulfate not only decreases the parts of sodium thiosulfate pentahydrate was then added amount of irreversible expansion suffered by the explosive to one of the compositions. Each of the compositions composition but also inhibits the reversible thermal exwas placed in a test tube filled to within about one half pansion acquired by the explosion compositions. inch of the brim and the tubes were then tightly stop- In order to test the effect of prolonged heating on the pered. The test tubes were then placed in a water bath explosive compositions of this invention, additional carmaintained at 98 C. The object of this experiment tridges containing Composition A were subjected to a was to determine the time necessary for the cork to be more rigorous test. After preparation, the cartridges forced out of the test tube because of the expansion of were first held at a temperature of 70 F. for 24 hours the nitrate-aluminum slurry. It was found that the comand the diameters measured. The temperature was then position which did not contain sodium thiosulfate exraised to 105 F., maintained for 24 hours, and therepanded sufiiciently so as to force the cork out of the after cooled to 72 F. for 24 hours. The temperature test tube 24 minutes after immersion in the water bath. was then raised to 92 F., maintained for 6% hours, and The composition embodying this invention, i.e., the comlowered to 66 F. for 18 hours. Thereafter, the carposition containing sodium thiosulfate had not expanded tridges were maintained at 125 F. for 24 hours and then sufficiently to force the cork from the test tube after at 66 F. for 24 hours. The temperature was then two hundred minutes, when the test was stopped. The raised to 113 F. for 17 hours and cooled to 66 F. for 7 same experiment was repeated, using 3 parts of anhydrous hours. The results are indicated in Table II. sodium thiosulfate in place of the 2 parts of the sodium Table 11 AVERAGE DIAMETER INCHES, AFTER HEATING, AT TEMPERATURE FOR TIME 24 hrs. at 6%,hrs. at 24 hrs. at; 17 hrs. at; Increase in diameter Cartridge Initial, 105 F., 92 13., 125 F., 113 F.,
No. 70 F. cooled to cooled to cooled to cooled to 72 F. 66 F. 66 F. 66 F. Total Percent These results show that the explosive compositions of this invention are capable of withstanding very severe storage conditions.
EXAMPLE 2 The following explosive composition was mixed as 'in Example 1:
Ingredient: Percent Nitrostarch 22.75 Mill ammonium nitrate 48.15 Mill sodium nitrate 14.25 Flake aluminum 2.00
Sodium thiosulfate (anhydrous) thiosulfate pentahydrate used previously. After 305 minutes, when the test was stopped, the cork had still not been forced from the test tube.
EXAMPLE 4 1.00 baths at 98 C. in order to determine the length of time *After this time, test was stopped without the cork having been forced from the tube.
This example shows that sodium thiosulfate and the dioctyl ester of sodium sulfosuccinic acid substantially inhibited thermal expansion of the composition. The coeificient of expansion of sodium nitrate varies with impurities in the batch, and this accounts for the fact that the composition in Example 3 forced the cork from the tube in 24 minutes, while the composition of the example required 85 minutes.
EXAMPLE 5 Two explosive compositions were prepared as in Example 1 of the following ingredients:
Parts by weight Ingredients Nitrostarch 7. 70 7. 70 Mill ammonium nitrate- 67. 20 67.20 M ll sodium nitrate... 13. 49 13. 49 Zinc oxide 0. 0. l0 Unbleached wheat flour 4. 00 4. 00 Anthracite coal 3. 00 3. 00 Flake aluminum. 0. 50 0. 50 Atomized aluminum. 1. 50 1. 50 Mineral oil (100 S S U 0. 0.20 Carbon black 0. 01 0.01 Sodium thiosuliate (anhydrous). 1. 50 Water 2. 2. 30
Compositions A and B were substantially identical in explosive properties, but Composition B was found to have negligible coeflicient of expansion, as compared to Composition A without sodium thiosulfate.
EXAMPLE 6 Two explosive compositions were prepared as in Example 1 of the following ingredients:
Parts by weight Ingredients Nitrostarch 12. 30 12. 30 Mill ammonium nitrate. 41. 00 41. 00 Coarse ammonium nitrate 25. 00 25. 00 Mill sodium nitrate 9. 04 9. 04 Zinc oxide 0. 20 0. 20 Unbleached wheat flour 3. 50 3. 50 Anthracite coal 2. 50 2. 50 Flake aluminum 1. 50 1. 50 Mineral oil (100 S.S.U. at 135 F.) 0.25 0.25 Carbon black 0.01 0. 01 Sodium thiosuliate (anhydrous) 1. 50 Water 5. 00 5. 00
The results indicated that Composition B was as good an explosive as the thiosulfate-free material A, but had a very low coeificient of expansion.
10 EXAMPLE 7 Two explosive slurry formulations were made up to the following formulations:
These formulations were packed in 1%" x 8" cartridges and subjected to storage tests cycling between temperatures of 86 to 106 F. for a period of 46 days. Following are the results of the tests:
Limit of Limit of variation variation Density 1.39 1.38 1.40 1. 36 Gain or loss in cc./volum +10 +10 +2 3 Percent expansion (86 F.) +6, 6 +6. 6 +1. 4 2. I
The results show that the sodium thiosulfate held expansion to a minimum under the test conditions.
EXAMPLE 8 Four explosive slurries were made up to the following formulation:
A B C D Ammonium nitrate, Monsanto Percent Percent Percent Percent E-2 prills 65. 25 65. 00 21. 50 21. 25 Sodium nitrate, mill 5. 00 5. 00 38. 00 3 8. 00 Aluminum granules (Almeg 0. ater 13. 00
Sodium thiosulfate (anhydrous) These formulations were packed in 1% x 8" cartridges and subjected to storage tests cycling between temperatures of 86 to 106 F. for a period of 46 days. Following are the results of the tests:
A B CID Gain or loss in cc./volume trom cc- +10 Percent expansion The results show that the sodium thiosulfate (B and D) prevented expansion under the test conditions.
EXAMPLE 9 An explosive mixture of semi-solid consistency (A in the table below) was prepared using nitrostarch, grained mill ammonium nitrate, mill sodium nitrate, flake aluminum, sodium benzene sulfonate, water and the additional ingredients noted in the table below. The nitrostarch, oil and mixed nitrates were thoroughly blended and were then added to the zinc oxide, flake aluminum, guar gum and sodium carboxymethyl cellulose. The sodium benzene sulfonate was dissolved in the water and then added to the mixture. The proportions compositions were as follows:
of the final explosive A B Ingredients Invention Control Percent Percent Nitrostarch 22. 75 22. 75 Mill ammonium nitrate 49. 65 48. 65 Mill sodium nitrate 14. 25 14. 25 Flake aluminum. 2. 2. 00 Zinc oxide 1.00 1.00 Sodium carboxymethyl cellulose 0. 60 0. 60 Guar gum 0. 50 0. 50 Sodium benzene sulfonate.- 1. 00 Water 9. 25 9. 25
These formulations were packed in 1%" x 8" cartridges and subjected to storage tests cycling between tempera tures of 68 to 106 F. for a period of 7 days. Following are the results of the tests:
Gain or loss in ec./volume from 165 cc 0 Percent expansion +3 0 organic sulfonates in an amount suflicient to inhibit the thermal expansion of the slurry.
2. An aqueous slurried explosive in accordance with claim 1 in which the sulfur compound is an inorganic thiosulfate.
3. An aqueous slurried explosive in accordance with claim 2 in which the thiosulfate is sodium thiosulfate.
4. An aqueous slurried explosive in accordance with claim 1 wherein the sulfur compound is an organic sulfonate.
5. An aqueous slurried explosive in accordance with claim 4 in which the sulfonate is an organic hydrocarbon sulfonate.
6. An aqueous slurried explosive in accordance with claim 4 in which the sulfonate is an ester-substituted hydrocarbon sulfonate.
7. An aqueous slurried explosive in accordance with claim 6 in which the sulfonate is an alkyl ester of sodium sulfosuccinate.
8. An aqueous slurried explosive in accordance with claim 1 in which the inorganic nitrate is ammonium nitrate.
9. An aqueous slurried explosive in accordance with claim 1 in which the inorganic nitrate is a mixture of ammonium nitrate and another inorganic nitrate.
10. An aqueous slurried explosive in accordance with claim 1 containing sufficient water to impart to the composition a semi-solid consistency.
11. An aqueous slurried explosive in accordance with claim 1 comprising a thickening agent in an amount to increase the consistency of the composition.
12. An aqueous slurried explosive in accordance with claim 1 comprising an explosive sensitizer.
13. An aqueous slurried explosive in accordance with claim 1 in which the slurrying liquid is water.
14. An aqueous slurried explosive in accordance with claim 1 in which the slurrying liquid is water and oil.
15. A method of reducing the coefiicient of thermal expansion of aqueous slurried explosive compositions comprising an inorganic nitrate oxidizer in an amount within the range from about 10 to about particulate aluminum in an amount within the range from about 0.5 to about 20%, and an aqueous liquid in an amount to form a slurry, which comprises incorporating therein a sulfur compound selected from the group consisting of inorganic thiosulfates and organic sulfonates in an amount sufiicient to inhibit thermal expansion.
References Cited by the Examiner UNITED STATES PATENTS 3,094,069 6/1963 Hradel 149--43 XR 3,111,437 11/1963 Hino et al. 149-46 3,116,185 12/1963 Wilson et al 14946 XR 3,121,036 2/1964 Cook et al. 149-41 3,147,163 9/1964 Grifliith et al 149-39 CARL D. QUARFORTH, Primary Examiner.

Claims (1)

1. AN AQUEOUS SLURRIED EXPLOSIVE COMPOSITON CHARACTERIZED BY A LOW COEFFICIENT OF EXPANSION WITH TEMPERATURE COMPRISING AN INORGANIC NITRATE OXIDIZER IN AN AMOUNT WITHIN THE RANGE FROM ABOUT 10 TO ABOUT 95%, PARTICULATE ALUMINUM IN AN AMOUNT WITHIN THE RANGE FROM ABOUT 0.5 TO ABOUT 20%, AN AQUEOUS LIQUID IN AN AMOUNT TO FORM A SLURRY, AND A SULFUR COMPOUND SELECTED FROM THE GROUP CONSISTING OF INORGANIC THIOSULFATES AND ORGANIC SULFONATES IN AN AMOUNT SUFFICIENT TO INHIBIT THE THERMAL EXPANSION OF THE SLURRY.
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Cited By (6)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
US3330706A (en) * 1966-02-08 1967-07-11 Trojan Powder Co Nitrostarch explosives containing slowly hydratable guar gum
US3337380A (en) * 1964-10-02 1967-08-22 Trojan Powder Co Explosive slurries from saturated ammonium nitrate solutions and process for preparing the same
US3369944A (en) * 1963-06-12 1968-02-20 Dynamit Nobel Ag Patentabteilu Thickened aqueous detonator composition containing a brisant explosive
US3471346A (en) * 1968-01-25 1969-10-07 Du Pont Fatty alcohol sulfate modified water-bearing explosives containing nitrogen-base salt
US20120305255A1 (en) * 2011-05-31 2012-12-06 Victor Borisovich Zavolzhskiy Method of Treating the Near-Wellbore Zone of the Reservoir
US10889751B2 (en) 2015-08-28 2021-01-12 Liberty Oilfield Services, LLC Reservoir stimulation by energetic chemistry

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Publication number Priority date Publication date Assignee Title
US3094069A (en) * 1959-01-05 1963-06-18 Dow Chemical Co Method of blasting and ammonium nitrate explosive composition
US3111437A (en) * 1960-01-09 1963-11-19 Nippon Kayaku Kk Cap sensitive ammonium nitrate-fuel oil explosive and a method of manufacturing the same
US3116185A (en) * 1960-08-18 1963-12-31 Phillips Petroleum Co Method of reducing the caking of nitrogen-containing compound
US3121036A (en) * 1958-02-28 1964-02-11 Canada Iron Ore Co Explosive composition comprising ammonium nitrate and a heat-producing metal
US3147163A (en) * 1960-08-25 1964-09-01 Trojan Powder Co Sensitized oil-slurried explosives

Patent Citations (5)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
US3121036A (en) * 1958-02-28 1964-02-11 Canada Iron Ore Co Explosive composition comprising ammonium nitrate and a heat-producing metal
US3094069A (en) * 1959-01-05 1963-06-18 Dow Chemical Co Method of blasting and ammonium nitrate explosive composition
US3111437A (en) * 1960-01-09 1963-11-19 Nippon Kayaku Kk Cap sensitive ammonium nitrate-fuel oil explosive and a method of manufacturing the same
US3116185A (en) * 1960-08-18 1963-12-31 Phillips Petroleum Co Method of reducing the caking of nitrogen-containing compound
US3147163A (en) * 1960-08-25 1964-09-01 Trojan Powder Co Sensitized oil-slurried explosives

Cited By (7)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
US3369944A (en) * 1963-06-12 1968-02-20 Dynamit Nobel Ag Patentabteilu Thickened aqueous detonator composition containing a brisant explosive
US3337380A (en) * 1964-10-02 1967-08-22 Trojan Powder Co Explosive slurries from saturated ammonium nitrate solutions and process for preparing the same
US3330706A (en) * 1966-02-08 1967-07-11 Trojan Powder Co Nitrostarch explosives containing slowly hydratable guar gum
US3471346A (en) * 1968-01-25 1969-10-07 Du Pont Fatty alcohol sulfate modified water-bearing explosives containing nitrogen-base salt
US20120305255A1 (en) * 2011-05-31 2012-12-06 Victor Borisovich Zavolzhskiy Method of Treating the Near-Wellbore Zone of the Reservoir
US9228424B2 (en) * 2011-05-31 2016-01-05 Riverbend, S.A. Method of treating the near-wellbore zone of the reservoir
US10889751B2 (en) 2015-08-28 2021-01-12 Liberty Oilfield Services, LLC Reservoir stimulation by energetic chemistry

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