US3661659A - Gelled acidic explosive compositions - Google Patents

Abstract

Gelling aqueous acidic compositions with a polymer having pendent amide or nitrile functions crosslinked by a monomer containing a plurality of amide or amine groups bonded to methylene or polymethylene through the amide or amine nitrogen, and a process for their preparation. The gelling system of this invention finds particular utility in explosive compositions based on an oxidizing agent and one or more fuels or sensitizers.

Description

United States Patent 51 3,661,659

Breza 1 May 9, 1972 [54] GELLED ACIDIC EXPLOSIVE 3,423,258 1/1969 Cross .149/19 COMPOSITIONS 3,451,868 6/ 1 969 Peterson 149/60 3,507,720 4/1970 Peterson ..149/19 [72] Inventor: Cyril J. Breza, Thorofare, NJ.

[73] Assignee: E. I. du Pont de Nemours and Company,

Wilmington, Del.

[22] Filed: Oct. 13, 1969 [21] Appl. No.: 865,983

[52] US. Cl ..149/19, 149/20, 149/44, 149/60, 149/61, 149/67, 149/74, 149/75, 149/76, 149/92, 149/93, 149/105 [51] Int. Cl. ..C06b 7/00 [58] Field of Search ..149/74, 19, 20, 75, 76, 57, 149/60, 61, 67, 69, 105, 44, 92, 93

[56] References Cited UNITED STATES PATENTS 3,361,601 6/1968 Chrisp ..l49/l9 Primary Evaminer-Carl D. Quarforth Assistant E.\aminerE. A. Miller Attorney-James .l. Flynn ABSTRACT Gelling aqueous acidic compositions with a polymer having pendent amide or nitrile functions crosslinked by a monomer containing a plurality of amide or amine groups bonded to methylene or polymethylene through the amide 0r amine nitrogen, and a process for their preparation. The gelling system of this invention finds particular utility in explosive compositions based on an oxidizing agent and one or more fuels or sensitizers.

9 Claims, No Drawings GELLED ACIDIC EXPLOSIVE COMPOSITIONS BACKGROUND OF THE INVENTION The handling of liquid acidic compositions has long been a complicating factor in their use in various industries such as .oil production, propellants, metallurgy, fertilizers and explosives, due to the inherent corrosiveness and, in some cases, strong oxidizing capacity of the acids. In more recent years, there has been increased interest in developing means of safely handling acidic compositions. This interest has been particularly evident in the explosives industry particularly with respect to compositions containing an inorganic oxidizing agent together with sensitizer or fuel components since the discovery of the greater work potential of water-bearing compositions containing these constituents. Since the constituents of such explosive compositions exhibit varying degrees of solubility, difficulty was encountered in maintaining the homogeneity of aqueous explosive compositions of this type. The use of such compositions for blasting in wet boreholes was still further complicated by the seepage of water into the explosive compositions, altering the constitution of the composition by dilution and leaching of the soluble components.

To help solve these problems, various thickeners or gelling agents have been used with slurried explosive compositions based on inorganic oxidizing salts. Satisfactory thickener systems for these compositions are based on natural hydroxylated polymers such as natural polysaccharides, particularly galactomannan gums and their derivatives.

The versatility of these systems is increased by the provision of various crosslinking agents which gel the compositions thereby increasing the stability of the system and usually imparting other beneficial effects. Some variations in product consistency is possible by varying the proportions of hydroxylated polymers and crosslinking monomers .in the compositions, but usually water-resistance is seriously deficient at concentrations low enough to provide readily pourable compositions. In particular there is a now well-recognized need for a gelling system for aqueous compositions which will provide stable, pourable compositions which exhibit good water resistance as well as being of use in forming the more conventional firm, highly viscous gels.

While the gelling systems of the prior art provide satisfactory performance for most aqueous compositions based on inorganic oxidizing salts which are to be of relatively high viscosity, renewed interest in explosives based on nitric acid, i.e., compositions sometimes referred to as Sprengel explosives, has presented new problems since the known thickening and gelling systems are not satisfactory in the strong acid. For example, explosives based on concentrated nitric acid as the primary oxidizing component exhibit exceptionally high acidity and oxidizing capacity which are particularly hazardous in fluid compositions. Further, the use of these compositions in wet conditions is accompanied by generation of high temperatures due to dilution of nitric acid with water. Gelling systems of the types used in compositions based on inorganic oxidizing salts tend to decompose under acidic conditions. In addition, these gelling systems in general require careful control of pH during formation, which control is not possible in the nitric acid based compositions, and are not operable in a highly acidic medium. Thickening of the nitric acid based compositions, e.g., by inorganic fillers or linear polymers, does not provide stable, cohesive, water resistant compositions having premium explosive properties.

Accordingly, there is still a need for aqueous acidic compositions having a gelling system which gives stable, water-resistant cohesive products ranging from pourable, yet water-resistant fluids to rigid gels.

SUMMARY OF THE INVENTION The instant invention provides an improvement in gelled aqueous acidic compositions which gives compositions of improved homogeneity, water-resistance and stability ranging from fluids to rigid gels. The improvement comprises a gelling system comprising the in situ crosslinked reaction product of at least one polymer containing a plurality of pendent groups selected from amide and nitrile functions, the amide nitrogen atoms bearing at least one hydrogen, and at least one monomer containing a plurality of amide or tertiary amine groups bonded to methylene or polymethylene through the amide or amine nitrogen. Preferably the polymer comprises about from 0.1 to 10 percent by weight of the acidic composition and the monomer comprises about from 0.005 to 5 percent by weight of the acidic composition. While the instant invention is useful for gelling various acidic compositions such as nitric acid, to facilitate their handling and use, it finds particular utility when used in conjunction with acidic explosive compositions comprising one or more fuels and an oxidizing component. This invention further provides a process for the manufacture of these gelled compositions which comprises bringing into contact, in an aqueous composition having a pH of less than about 6.0, at least one polymer containing a plurality of pendent substituent groups selected from amide and nitrile functions, the amide nitrogen atoms bearing at least one hydrogen, and at least one monomer containing a plurality of amide or tertiary amine groups bonded to methylene or polymethylene through the amide or amine nitrogen.

DESCRIPTION OF PREFERRED EMBODIMENTS The gelling system of this invention can be used with a wide range of acids including the common mineral acids such as nitric acid, perchloric acid, sulfuric acid, hydrochloric acid, and phosphoric acid and water soluble or miscible organic carboxylic acids having a dissociation constant in water of at least about 1 X10 such as lower aliphatic monocarboxylic acids. These can include, for example, formic, acetic, propionic, butyric or isobutyric acid and lower aliphatic diand poly-carboxylic acids of 2 to 7 carbon atoms such as oxalic acid, malonic acid, succinic acid, and glutaric acid. The pH of the acidic compositions is less than about 6.0 and preferably less than about 5.5. Of the above-named acids, the mineral acids and salts derived therefrom whose aqueous solutions are acidic, e.g., ammonium nitrate, are particularly well suited for forming the gelled structures of this invention. In gelling organic acids and aqueous solutions of salts derived therefrom, the presence of small quantities of a mineral acid is used to speed gelation. Aqueous nitric acid and aqueous solutions of ammonium nitrate are particularly preferred acidic compositions to be gelled in accordance with this invention since, as will be described and exemplified more fully hereinafter, there is a particular utility for these inter alia in the formulation of explosive compositions. Nitric acid of about from 5 to 99 percent strength can be used; but nitric acids having concentrations of greater than 50 percent are most often used, and concentrations of about from 65 to 98 percent are particularly preferred.

In addition to its usefulness in gelling substances which are considered as acids per se, the gelling system of this invention also finds utility with aqueous acidic solutions of compatible substances. Examples of such substances include: ammonium nitrate, ammonium perchlorate, ammonium chlorate, ammonium sulfate, ammonium bisulfate, and ammonium phosphate and solutions or suspensions of other compositions, e.g., sugar, which have been made acidic.

In this specification the term lower alkyl means an alkyl radical of from 1 to four carbon atoms, unless otherwise indicated.

Polymers which can be used in accordance with this invention include, for example,

1. polymers of which at least about 2 percent of the units are Til wherein X is selected from CN and wherein R is as defined above.

Examples of such polymers which are especially suitable for use in accordance with this invention from the viewpoint of solubility and dispersability in the liquid phase of the acidic compositions and availability at reasonable cost include poly(acrylic amides) which are polymers of acrylamide or methacrylamide, polymers of N-substituted derivatives of acrylic amides such as N-methylacrylamide, N-ethylacrylamide, and N-methylmethacrylamide, and polymers of hydroxyalkyl derivatives of amides such as a,2-hydroxyethyl acrylamide and a-hydroxymethacrylamide. Examples of poly(acrylic nitriles) which can be used in this invention include polymers of acrylonitrile, methacrylonitrile, a-butylacrylonitrile, and a-hydroxymethacrylonitrile. In general, homopolymers of the above mentioned acrylic amides or nitriles or their mutual copolymers are preferred polymers because of their low cost and ease of dissolution in a wide range of acidic liquids. Particularly preferred polymers are homopolymers of acrylamide and of acrylonitrile and copolymers of acrylamide and acrylonitrile in ratios varying about from 1/20 to 20/1. Copolymers comprising at least about 2 percent of amide or nitrile units as defined above and the balance other copolymerized units can also be used. Representative copolymerizable monomers include acrylic monomers, e.g., acids such as acrylic acid, methacrylic acid, methyl acrylic acid and a-propyl acrylic acid; esters such as methyl acrylate, methyl methacrylate, ethyl acrylate, n-butyl methacrylate and n-hexyl acrylate; cycloalkyl substituted acrylics, e.g., cyclohexyl methacrylate; salts such as sodium or ammonium acrylate or alkyl ammonium acrylates; hydroxyalkyl acrylates, e. g., 2-hydroxyethyl acrylate or 2-hydroxypropyl acrylate; cyanoalkyl acrylics such as acyanoethylacrylonitrile; nonacrylic monomers such as sodium styrene sulfonate, vinyl acetate, vinyl pyridine and vinyl pyrrolidone and mixtures of two or more of such monomers, providing the copolymer formed meets the solubility and stability requirements set forth. Although low concentrations of monomers having pendent amide or nitrile functions in the copolymers can sometimes be used, e.g., as low as l to 2 percent, these monomers usually will comprise at least about 2 percent of the copolymer. Preferred polymers include vinyl addition polymers soluble in the systems used herein, preferably having a molecular weight of about from 50,000 to 6 million.

crosslinking monomers which can be used in accordance with this invention can be selected from compounds having a plurality of amide or tertiary amine groups bonded to methylene or polymethylene through the amide of amine nitrogen. In general, the tertiary amine groups can be represented by the formula R N-, where the R's are any organic radicals and can be the same or different, and the amide groups can be represented by the formula K il l consisting of lower alkyl, cycloalkyl, hydroxyalkyl, aryl, aralkyl, alkenyl, and aralkenyl radicals of l to 8, and preferably l to 4, carbon atoms. In the preferred amide groups, the R's are independently selected from the group consisting of hydrogen and lower alkyl, cycloalkyl, hydroxylaklyl, aryl, aralkyl, alkenyl and aralkenyl radicals of l to 8, and preferably 1 to 4, carbon atoms.

Representative monomers that are suitable for use in this invention include, for example, polyamide methylenes, such as N,N-methylenebisformamide, N,N-methylenebisacetamide, N,N'-methylenebisacrylamide and N,N-methylenebisbutyramide, polyamide polymethylenes, such as N,N'- bimethylenebisformamide, N,N'-trimethylenebisformamide, N,N'-hexamethylenebisformamide, and N,N-hexamethylenebisacrylamide, cyclic methyleneamines, such as cyclohexamethylenetetramine, and mixtures of two or more of the above.

Of the above illustrative crosslinking monomers, N,N- methylenebisacetamide, N,N-methylenebisacrylamide, N,N'- hexamethylenebisacrylamide and cyclohexamethylenetetramine are preferred, with N,N'- methylenebisacetamide and N,N-methylenebisacrylamide being especially preferred, for the compositions of the instant invention.

The term soluble in the aqueous acidic component" and similar terms as used herein, refers to components having appreciable solubility at ambient temperatures, i.e., about 20 to 25 C., in the particular aqueous, acidic component to be gelled. In general, this solubility should be at least about 10 percent by weight and preferably appreciably greater, e.g., 50 percent or more. The reaction between acrylic polymer and crosslinking monomer should not preferentially form products which separate, e.g., by precipitation, from the aqueous acidic composition or agglomerate into flocculates or lumps. Crosslinking of the polymer chains forms a structure which is a gel rather than a precipitate. This gelled structure swells in and holds the aqueous, acidic composition and is of substantially constant composition throughout. The gelled crosslinked structure contains a relatively low ratio of polymer solids to liquid phase, e.g., less than about 1 to 10, this ratio being roughly equal to the weight ratio of combined polymer and monomer to the liquid phase, in contrast to precipitates or agglomerates in which there is a high ratio of polymer solids to liquid phase.

The gelled compositions of this invention are stable. That is, there is little or no degradation of the polymer, crosslinking monomer or their reaction products in the aqueous acidic composition to be gelled. Since prolonged stability is particularly desirable, stability refers particularly to absence of degradation of a crosslinked system when subjected to accelerated thermal stability tests which involve heating the sample at a temperature of 50 C. (122 F.) for a period of at least 8 to 12 hours.

Strength, when used herein with regard to acids, particularly to nitric acid, expresses in percent the relationship between the weight of percent (dry) acid and the weight of acid plus water in the particular acid.

The polymer for the gelling system preferably is provided as preformed polymer. However, if desired, the polymer can be formed in situ in the acidic liquid in the presence of free-radical polymerization initiators which are soluble to the extent of at least about 0.1 percent in the acidic liquid. Suitable initiators include sodium, potassium and ammonium salts of inorganic peracids; hydrogen peroxide; and organic peroxide and azo catalysts. Generally, persulfates are preferred. The persulfate ions, which are introduced as a soluble persulfate salt, can be used alone in the solution of inorganic oxidizing salt to promote the polymerization reaction or an added reducing agent can also be employed to form a redox couple.

The amide monomers employed for in situ polymerization in the gelled compositions of this invention need not be highly purified. For example, crude acrylamide sulfate obtained by the hydrolysis of the corresponding nitrile, acrylonitrile, in the presence of concentrated mineral acid, e.g., sulfuric acid, can

be used directly without purification. The presence of the minor residual amounts of mineral acid in the crude monomer catalyzes the crosslinking reaction making possible faster gel times and exerts no detrimental effect in the explosive composition. Additional acid, such as sulfuric acid, can be added in amounts of about from 0.5-5 percent as a positive catalyst to hasten gelling of the aqueous phase of the compositions.

Preformed polyacrylamides which can be used in this invention include Cyanomer" P-250, commercially available from American Cyanamide and Polyhall 295M commercially available from Stein Hall. Particularly preferred polyacrylonitriles are those commercially available from Du Pont and sold under the trademark Orion Acrylic Fiber, and those prepared by emulsion polymerization techniques according to Sorenson and Campbell, Preparative Methods of Polymer Chemistry, p. 169. Preferred copolymers consist of 2 to 25 percent acrylamide and 98 to 75 percent acrylonitrile prepared by emulsion polymerization in accordance with En cyclopedia of Polymer Science and Technology, Vol, I, p. 400; these copolymers have intrinsic viscosities in 0.1 percent solutions in dimethylformamide at 30 C. of 8.0 to 10.0. Gels of very desirable properties can be formed from lower molecular weight polymers but higher molecular weight polymers form gels more rapidly at lower temperatures and, in addition, usually require the use of less crosslinking monomer to provide gels of equivalent properties, other ingredients and conditions remaining the same.

Preparation of the gelled compositions of this invention can be accomplished by simply incorporating the polymer (preformed or formed in situ) and crosslinking monomer into the liquid acidic medium. There is no need for any catalyst and reaction between the polymer and crosslinking monomer in most cases begins shortly (within seconds) after addition of the polymer and monomer. Usually the polymer is admixed with the acidic composition and the crosslinking monomer subsequently added to the composition.

In general, gels form more rapidly when heat, e.g., of about from 30 to 80 C., is applied than when the reaction is carried out at or near ambient room temperature. However, when the acidic composition is also a strong oxidizer and particularly when it is nitric acid, heating to temperatures above about 50 C. preferably should be avoided. In the preparation of blasting compositions based on aqueous solutions of inorganic nitrate it is particularly convenient to use concentrated aqueous solutions of ammonium nitrate commonly known in the art as ammonium nitrate liquor, the aqueous liquid phase of the composition being provided for the most part by this solution. In forming the gelled compositions of this invention care should be taken that all ingredients, viz, the polymer, crosslinking monomer and, if desired, any solid to be dispersed in the gel, are uniformly dispersed through the composition. Agitation used for blending and dispersing of components is desirably continued until the composition is gelled, particularly when particulate solids for example, fuels or sensitizers such as TNT, smokeless powder and/or aluminum used in explosive compositions, are to be distributed uniformly through the gel matrix. In some instances, for example, in explosive compositions which are to contain a high percentage of solid TNT or when a solid which inhibits polymerization or the crosslinking reaction is to be incorporated in the compositions, all ingredients except such additives can be mixed and gelled and such additives blended into the gel formed.

When the polymer is to be formed in situ, the rate of polymerization and, in some instances, product consistency can be adversely affected by the presence of nitrogen oxides and oxygen, either in dissolved form or as the gases, and by the presence of large amounts of compounds conventionally used to inhibit free-radical polymerizations of the monomers. Compensations for these variations can be provided, when necessary, by increasing the concentrations of polymerization promoters. An alternative and generally more economical expedient, however, is to reduce the concentrations of these polymerization-retarding components prior to the polymerization. In the case of nitrogen oxides and oxygen, this can be accomplished by carrying the polymerization out under a blanket of an inert gas, typically nitrogen. To further eliminate polymerization inhibiting concentrations of nitrogen oxides and/or oxygen, the components of the gelled composition, particularly the aqueous solution of inorganic oxidizing salt, can be sparged with the inert gas. When preformed polymer is used, as is preferred, there is no need to sparge the components.

The rate of gelling and the viscosity of the gelled compositions of this invention can be varied according to the needs of a particular application. In general, the rate of gelling and the viscosity of the gel can be increased by increasing the percentage of polymer in the system, by increasing the relative proportion of crosslinking monomer used for a given quantity of the polymer, by increasing the molecular weight of the polymer employed in the system, or any combination of the above.

Several of the gelled acidic compositions based on nitric acid or an oxidizing salt are inherently satisfactory as detonating explosives without further additives, i.e., they can be detonated with moderate-strength primers in diameters of 6 inches or less under moderate conditions of confinement, such as provided by a borehole or a container of moderate wall thickness. However, for explosive applications, the compositions of this invention also preferably contain one or more fuels and/or sensitizers which are stable in the acid of the strength used in preparing the gels. Examples of non-explosive fuels are the monoand dinitro aromatic hydrocarbons, such as nitrobenzene, o-mononitrotoluene and dinitrotoluene; liquid and solid hydrocarbons and hydrocarbon fractions, particularly refined petroleum and mineral oils and the aromatic hydrocarbons, such as benzene, toluene, and the xylenes; carbohydrates, including various cellulose and starch products, e.g., cornstarch, potato starch, wood and paper pulps and sugar; siliceous fuels, including silicon itself and mixtures and alloys of silicon with heavy metals, e.g., ferrosilicon; and sulfurous fuels such as sulfur itself and pyrites. Metal fuels such as aluminum or ferrophosphorus are also useful in some of the gelled compositions, provided that they are, or can be made, sufficiently resistant to attack by the nitric acid. The gel copolymer per se acts as a fuel and except as otherwise indicated is included in calculating the amount of non-explosive fuel and oxygen balance. Ordinarily, the gels for use as explosive compositions will be formulated to have an oxygen balance of about from 25 to +10 percent.

In addition to the non-explosive fuels and/or sensitizers named above the explosive compositions of this invention can, in some embodiments, contain one or more additives of the art-recognized self-explosive type, provided that such additive is stable in the strengths of acidic composition used in preparing the gels. TNT, for example, exhibits a high degree of stability in all strengths of aqueous nitric acid and ammonium nitrate liquors and hence is a particularly useful additive of the self-explosive type. Examples of other self-explosive" components which can be used in the compositions of this invention are RDX, HMX, tetryl, PETN, nitrocellulose, smokeless powder, and other organic nitramines, nitrates and nitrocompounds. For reasons of economy and compatibility, TNT is the preferred self-explosive for use in the compositions of this invention. The TNT or mixtures thereof (e.g., with ammonium or sodium nitrate) can be introduced into the compositions in the form of crystals, grains, pellets, flakes, or other particulate form which allows ready dispersion thereof. In general, up to percent, and preferably up to 40 percent, by weight of self-explosive additive based on weight of the composition can be used.

Stable, gelled nitric acid compositions found especially economical and efiicient as detonating explosives comprise a uniform blend of:

a. about from 25 to percent by weight of aqueous nitric acid having a strength of about from 50 to 99 percent, and preferably 65 to 98 percent;

b. about from to 30 percent of a non-explosive fuel, preferably selected from siliceous fuels, light metals, liquid and solid hydrocarbons, carbohydrates, sulfur, monoand dinitro aromatic hydrocarbons, and mixtures of such fuels and/or sensitizers;

c. up to about 40 percent of a self-explosive sensitizer, particularly TNT;

d. up to about 50 percent of an inorganic oxidizing salt, typically an inorganic nitrate; and

e. an in situ polymerization product of 1. about from 0.1 to percent and preferably 0.2 to 5 percent, based on the weight of aqueous nitric acid of at least one polymer as defined above, which preferably is formed from acrylamide, acrylonitrile, methacrylonitrile, or methacrylamide or is a copolymer of monoethylenically unsaturated monomers of this group, and

(2) about from 0.005 to 5 percent and preferably 0.01 to 2 percent by weight based on the weight of aqueous nitric acid of a crosslinking monomer as defined above, and preferably N ,N'-methylenebisacetamide or N,N- methylenebisacrylamide.

Particularly preferred explosive compositions based on inorganic oxidizing salts and having an oxygen balance of about from 25 to +10 percent comprise:

a. about from 20 to 70 percent ammonium nitrate;

b. up to 40 percent and preferably 10 to 25 percent sodium nitrate;

c. up to 40 percent and preferably 10 to 30 percent self explosive;

d. up to 30 percent of metallic fuel, preferably 2 to 20 percent of aluminum and/or 5 to 25 percent offerrophosphorus;

e. up to 10 percent of non-explosive fuel, preferably selected from carbonaceous, siliceous or sulfurous fuels or combinations thereof;

f. from 5 to 45 percent and preferably 10 to 30 percent of water;

g. an in situ formed product of I. about from 0.1 to 10 percent and preferably 0.2 to 5 percent based on the weight of the aqueous phase of the composition of at least one polymer as defined above, and preferably a poly(acrylic amide) and 2. about from 0.005 to 5 percent based on the weight of the aqueous phase of the composition of a crosslinking monomer as defined above, which monomer is preferably, N,N-methylenebisacetamide or N,N- methylenebisacrylamide.

In general, the gelled blasting compositions of this invention are prepared by blending of the ingredients, e.g., in a rotary type mixer such as a Lightnin AG-IOO mixer, keeping in mind the same general considerations for the control of the process as were discussed above. As mentioned, it is generally preferred to use preformed polymer to avoid the need for sparging and for maintaining the components while being blended under an inert gas atmosphere until polymerization is complete. Usually, the nitric acid is introduced into the mixing vessel first and the other ingredients added individually thereto while the contents of the vessel are being agitated. The crosslinking monomer is usually the last ingredient added. Agitation can be continued until after the composition is gelled, particularly when the added fuels or sensitizers are solids such as for example, ferrosilicon, sulfur, aluminum, silicon, or starch, which must be distributed uniformly throughout the gel matrix. Where fuels or other additives of marginal stability or additives which inhibit polymerization are to be incorporated in the compositions, all ingredients except such additives can be mixed and gelled as previously described, then such additives blended with the finished gel.

As indicated above, for explosive applications preferred ranges of nitric acid strength are about from 60 percent (corresponding to a maximum water content of about 40) to 97 percent. In general, the unit or bulk strength of an explosive composition based on gelled nitric acid increases with increasing strength of the nitric acid gelled. Accordingly gels of nitric acid of percent strength or higher are usually employed where high bulk strength is a requisite, e.g., in the bottom ofa borehole. The bulk or unit strength of an explosive composition, its relative ease of initiation, and its minimum critical diameter can also be regulated to a large degree by the type and quantity of fuel and/or sensitizer employed. Organic nitro compounds, typically mononitrotoluene, or dinitrotoluene, or in particular a self-explosive composition, especially TNT, are incorporated to provide compositions which are easily initiated, e. g., by a relatively small primer or by a blasting cap, in some cases, in small diameters. In many cases, a combination of fuels will be employed within the range of proportions indicated to give a composition having the desired physical and explosive properties.

Preferred gelling systems for explosive compositions comprise polymers of acrylonitrile, acrylamide, methacrylonitrile or methacrylamide, or copolymers thereof. The crosslinking monomer preferred is N,N-methylenebisacetamide or N,N'- methylenebisacrylamide. In addition to being readily available at reasonable cost, these compositions are particularly effective in providing firm cohesive gels having viscosities within the desired range of 100,000 to 10 million cps, high surface tension as evidenced by lack of stickiness or tackiness, ready workability, flexibility, water resistance, and other desirable physical characteristics in the as-made state. Further compositions including these preferred gelling systems retain their initial physical and explosive properties during storage after production. The preferred gelling systems also allow relatively wide latitude in the consistency of the explosive product made to fit the needs of a particular type of blasting.

This invention therefore provides simple and effective modified aqueous acidic compositions which are easier and safer to handle than those known heretofore and which have controlled free acidity and excellent stability. These and other properties of the gelled acidic compositions of this invention make the products of this invention particularly suitable as propellants, cleaning solutions, oil well treating agents, and etching compositions, in chemical syntheses, as an acidifying agent in mineralogical processes, in fertilizers, and in other uses where aqueous acid is now employed. In addition, physical properties such as cohesiveness, controlled flexibility and consistency and the ability to maintain dispersion of solids therein as well as their explosive properties make compositions of this invention, particularly those containing conventional fuels and sensitizers, readily adaptable to formulation in fixed plant facilities as well as mobile and other on-site equipment.

The gelled compositions based on an inorganic oxidizer can be employed for a variety of applications in which liquid aqueous acidic compositions are ordinarily employed, as an acidifying agent in mineralogical and other processes, in preparing salts, and in like operations. The gelled nitric acid compositions find particular merit as an oxidizing or nitrating acid in chemical synthesis in such applications when delayed action is desirable or required; inasmuch as the gels tend to release the acid slowly.

In the following examples which further illustrate this invention, parts, percentages and ratios are by weight unless otherwise indicated.

EXAMPLES 1-28 Gelled aqueous acid compositions of this invention are prepared from the materials noted in Table I. The polymer and any additives are first dissolved and admixed in the acid of the strength indicated and the crosslinking monomer is then added with agitation, which is continued until dissolution of the monomer and polymer is substantially complete. Then the mixture is allowed to gel. The reaction temperature is as noted in the table. Gelation time refers to the interval of time between the addition of the last ingredient and the completion of the gelling. None of the gel products shown visible signs of deterioration at ambient temperatures (20-25 C.) over periods of 1 week, the maximum periods of observation. In the Examples, the polyacrylamide used is Cyanomer" P-250, commercially available from American Cyanamide Co. with a molecular weight of 5-6 million, and the polyacrylonitrile is Orion Acrylic Fiber with molecular weight of 50,000-70,000 commercially available from E.I. du Pont de Nemours and Company.

TABLE I Aq. avid/strength pereent Crosslinking monomer I Temp, Time to gel Example parts Polymer parts parts Additives parts C. (hrs-min.)

1 liNO3/75, 08.6 Polyacrylonitn'lc, 1.2 N,Ngmethylene-bisacryla- 21 16 mi e, 0.2. 2 1INOa/75, 08.6 .do N,N'-hexamethylene-bis- 21 484) aerylamide, 0.2. 3 I1NO3/75, 77.4 Polyacrylonitrilc, 1.00 N,N-met.hylerw-hisacryl- Nitl'olienzene, 21.50... 38 3- 0 amide, 0.1. 4 IINO3/75, 77.45 "do N,N-metl1ylene-l)isaeryl- (l0..... 38 12 0 amide, 0.05. 5 I1NO3/75, 77.47 ..(1o N,N-methyle||eliisaeryl ll 3X 30 0 amide, 0.03. 0 llNO3/75, 77.45 do V N,N'-methylelle-liisaeryl- 110..." 13 4X 0 amide, 0.05. 7 1INO;;/75, 77.47 .410 N,N-meLl|ylvne-bisaei'yl- .(lu 13 00 0 amide, 0.03. 8 1lNO /75, 77.40 Iolyaerylonitrile, 1.50.. N,N'-methylvi\e-liisaeryl- Nlllfllillllllll, 21.00. 21 16 0 amide, 0.10. 0 llNOz/75, 77.45 (lo N,N-n1ethyIeue-liisael'yl- (lo. '21 36 0 amide, 0.05. 10 llN0 /75, 77.40 1o V N,N-metl|yleiie-liisaeryl- "410 l2 -1041 amide, 0.10. 11 1INO /75, 77.40 do V v .(lo V V 1 (10 13 120*0 12 1lNO1/75, 08.0 lolyacrylamidc, 1.2 N,N niethyIene-bisaeryl- 21 2-0 ami e, 0.2. 13 IINO3/75, 08.6 d0 Cyclohexamiethyl-lenetet- 21 0-4 ramine, 0.2. 1-1 1lNO3/75, 83.6 Polyacrylonitrile, 1.2 H N,N-(r1nethy1en-bisacryl- Nltrobenzene, 15.0. 21 16-0 ami e, 0.2. llNO;i/75, 83.0 Poylacrylamide, 1.2 d0 (l0 21 10-0 10 llNO /75, 88.6 00/10 copolymer of ac ryl- .do ..(l0 21 10-0 amide and acrylonitrile, 1.2. 17 Acetic acid/75, 06.0, IICI/ Polyaerylamide, 1.2 do 21 24-0 100, 2.0. 18 11Cl/37, 08.6 do 21 10-0 10 31/0 NI14NO3/NaNOa/80, do 71 030 06.6, IICl/IOO, 2.0. 20 31/0 NH4NO3. NHNOJ/SO, .do Cyclohexamethyl lenetet- 71 03 06.6, I1Cl/100, 2.0. ramine, 0.2. 21 31/0 N1'I NO3/NaNO3/80, do N,N-methyleneliisaect- 71 0-1 07.6, IICl/IOO, 1.0. amide, 0.2. 31/0 NII NO3/NaNO3/80, do "do 7 0-3 08.4, llCl/l00, 0.2. 33 Nll NOa/65, 07.8, 1ICl/100, do r d0 21 43-0 0.8. 14 Nll4NO3/G5,07.8,IICl/100, do do 71 0-8 0.8. NII4N03, 07.0, IIgSO4/100, do .110 71 1.0. 26 lIN03/75, 08.6 do "do 21 48-0 "7.. 1lNO3/75, 08.6

EXAMPLES 29-38 The gelled compositions from Examples 3-11 are tested for detonation properties by transferring the gells to 2-inch diameter, 200 g. containers and initiating them with No. 8 electric blasting caps. All samples detonate.

What is claimed is:

1. A process for making stable, gelled aqueous acidic explosive compositions which comprises bringing into contact, in an aqueous composition having a pH of less than 6, oxidizing component, fuel and water, and

a. at least one polymer containing a plurality of pendent substituent groups selected from amide and nitrile functions, amide nitrogen atoms bearing at least one hydrogen, and

b. at least one monomer containing a plurality of amide or tertiary amine groups bonded to methylene or

Claims (7)

1. 2. A process of claim 1 wherein the polymer comprises about from 0.1 -10 percent by weight of the total composition and said monomer comprises about from 0.005-5 percent by weight of the total composition.
2. 3. A process of claim 2 wherein the polymer comprises polyacrylamide.
3. 4. A process of claim 2 wherein the polymer comprises polyacrylonitrile.
4. 5. A process of claim 2 wherein the monomer comprises N,N''-methylenebisacetamide or N,N''-methylenebisacrylamide.
5. 6. A process of claim 2 wherein the oxidizing component is nitric acid. 7. A process of claim 6 wherein the polymer is polyacrylamide and the monomer is N,N''-methylenebisacrylamide or N,N''-methylenebisacetamide.
6. 8. A process of claim 6 wherein the polymer is polyacrylonitrile and the monomer is N,N''-methylenebisacrylamide or N,N''-methylenebisacetamide.
7. 9. A process of claim 2 wherein the oxidizing component is ammonium nitrate.