Production of explosive emulsions

Claim 2

A process for producing explosive emulsion compositions sensitized with microbubbles comprising: (a) forming an aqueous inorganic oxidizing salt solution of at least about 64% by weight inorganic oxidizing salts and maintaining said solution above the crystallization temperature thereof; (b) forming a hydrocarbon fuel component and heating it to approximately the same temperature as said oxidizing solution; (c) introducing said oxidizer solution, said hydrocarbon fuel component, and an emulsifier to a mixing zone and mixing at conditions sufficient to obtain emulsifying shear rates to thereby form an emulsion matrix, said emulsifier being added in a manner such that the time of contact with the heated oxidizer solution and hydrocarbon fuel component is not sufficient to cause said emulsifier to degrade prior to the formation of said emulsion matrix; and (d) blending with said emulsion matrix a predetermined quantity of microbubbles delivered from a deaerated supply thereof to form explosive emulsion.

Claim 3

The process of claim 1 wherein said oxidizing salt solution is maintained at a temperature of about 187 degrees F.

Claim 4

The process of claim 1 and further comprising blending with said emulsion matrix a particulate metal.

Claim 5

The process of claim 3 wherein said particulate metal is particulate aluminum.

Claim 6

The process of claim 1 and further comprising filtering said aqueous inorganic salt solution and said hydrocarbon fuel component prior to introduction into said mixing means.

Claim 7

The process of claim 1 wherein said emulsifier is added to said hydrocarbon fuel component and dispersed therein at a point prior to introduction of said hydrocarbon fuel component to said mixing means.

Claim 8

The process of claim 1 wherein said microbubbles are delivered from said deaerated supply thereof for blending with said emulsion matrix on the basis of a predetermined weight percent of microbubbles, based on the weight of the explosive emulsion.

Claim 9

The process of claim 1 wherein said microbubbles are delivered from said deaerated supply thereof for blending with said emulsion matrix on the basis of a predetermined volume thereof to obtain explosive emulsions of a predetermined density.

Claim 10

The process of claim 1 wherein said mixing means is a continuous recycle mixer.

Claim 11

A process for producing cap sensitive water-in-oil explosive emulsion compositions sensitized with microbubbles comprising: (a) filling an oxidizer solution holding tank with an aqueous solution of inorganic oxidizing salts comprising at least about 67% of weight of said inorganic oxidizing salts and maintaining said solution at a temperature above about 187 degrees F; (b) filling a fuel component holding tank with a quantity of hydrocarbon fuel component and heating said hydrocarbon fuel component to substantially the same temperature as said oxidizer solution; (c) simultaneously passing controlled proportions of said oxidizing component and said fuel component to a mixing zone, adding an emulsifier to said fuel component at a point just prior to said mixing zone such that said emulsifier is not degraded from contact with said heated hydrocarbon fuel; (d) mixing said oxidizer solution, hydrocarbon fuel, and emulsifier components in said mixing zone at conditions sufficient to obtain emulsifying shear rates to form an emulsion matrix; and (e) blending with said emulsion matrix a predetermined quantity of microbubbles to thereby form said cap sensitive water-in-oil composition.

Claim 12

A process for producing cap sensitive water-in-oil explosive emulsion compositions sensitized with microbubbles comprising: (a) filling an oxidizer solution holding tank with an aqueous solution of inorganic oxidizing salts comprising at least about 67% of weight of said inorganic oxidizing salts and maintaining said solution at a temperature above about 187 degrees F; (b) filling a fuel component holding tank with a quantity of hydrocarbon fuel component and heating said hydrocarbon fuel component to substantially the same temperature as said oxidizer solution; (c) simultaneously passing controlled proportions of said oxidizing component and said fuel component to a mixing zone, adding an emulsifier to said fuel component at a point just prior to said mixing zone such that said emulsifier is not degraded from contact with said heated hydrocarbon fuel; (d) mixing said oxidizer solution, hydrocarbon fuel, and emulsifier components in said mixing zone at conditions sufficient to obtain emulsifying shear rates to form an emulsion matrix; and (e) blending with said emulsion matrix a predetermined quantity of microbubbles to thereby form said cap sensitive water-in-oil composition.

Claim 13

The process of claim 10 and further comprising blending with said emulsion matrix a predetermined amount of a particulate metallic fuel component.

Claim 14

The process of claim 11 wherein said particulate metallic fuel component is particulate aluminum.