Process for coating crystalline explosives with polyethylene wax
AssigneeThe United States of America as represented by the Secretary of the Navy
InventorVernon D. Ringbloom
Life of this patent
Estimating the term…
Loading patent…
AssigneeThe United States of America as represented by the Secretary of the Navy
InventorVernon D. Ringbloom
Estimating the term…
An improved method of coating crystalline high explosives with polyethylene ax comprising: (a) forming a loose slurry of finely divided crystalline explosive particles in water; (b) adding an emulsion of (1) an emulsifiable polyethylene wax, (2) potassium stearate, (3) KOH, and (4) water to the slurry; (c) heating the slurry-emulsion mixture to a temperature in the range of from about 92.degree. C. to about 98.degree. C. with stirring; (d) adding enough acetic acid to the slurry-emulsion mixture to lower the pH to about 6 with stirring; (e) cooling the resulting solution; and (f) isolating the product polyethylene wax coated high explosive particles.
A method of coating explosives with polyethylene wax comprising the steps of
Dependencies are inferred from the claim text.
Drawings are temporarily unavailable. Open the PDF at USPTO
No related US applications are recorded in the indexed filing history.
The component base containing an organic explosive or an organic thermic component: the coating containing an organic compound
Apparatus or methods for working-up explosives, e.g. forming, cutting, drying: treatment of solid structures, e.g. for coating or impregnating…
Compositions characterised by non-explosive or non-thermic constituents: fillers, gelling and thickening agents , absorbents for nitroglycerine
Explosives or thermic compositions
Term ended 20 May 2001 (estimated)
USPTO file history isn’t available for this patent, so only indexed dates are shown.
This invention relates to explosives and more particularly to polymeric wax coated explosives.
Previous methods of coating crystalline high explosives use polyethylene wax emulsified with fatty acids and basic materials such as ammonia and morpholine. The explosive crystals are then slurried in the aqueous emulsion. The emulsion is then broken with a heavy metal salt such as BaCl.sub.2 thus freeing the polyethylene particles to coat the explosive crystals. After the particles are coated and the mixing operation is completed, the remaining water is removed and the coated crystals are washed. The effluent water from this process contains Ba.sup.++ ions which are highly toxic and quite costly to remove. The Ba.sup.++ ions must be removed before the effluent water can be disposed of in the conventional manner.
According, an object of this invention is to provide a new method of coating high crystalline explosives with polymeric waxes.
The emulsions used in the present process are composed of a polyethylene wax, potassium stearate as an emulsifier, KOH, and water. The waxes used are low molecular weight, emulsifiable polyethylene waxes which soften at temperatures of less than 100.degree. C. They are soft, pressable polyethylene waxes. Examples of suitable waxes are sold by Allied Chemical Company under the trademark AC-656.TM. and by Eastman Chemical Company under the trademark Empolene 110.TM..
The ratio of water to polyethylene wax in the final emulsion may be from about 99:1 to 1:1. In other words, the weight percentage of polyethylene wax based on the weight of the wax plus water is from about 1.0 to 50.0. The higher percentages of wax make transportation and storage more convenient. A 1:1 ratio of water to wax (i.e., 50 weight percent wax) works well; however, it is possible that emulsions having much greater polyethylene wax contents would be difficult to dilute with water as requiring later in the process. Emulsions with low percentages of wax are used when a thinner coating of wax is desired. For most purposes a weight percent of from 10 to 30 is preferred, with 15 to 25 being more preferred. In other words, a weight ratio of water to polyethylene wax of from 9:1 to 2.33:1 is preferred, with from 5.67:1 to 3:1 being more preferred.
The emulsifier used is preferably potassium stearate. Generally, stearic acid is added to the mixture and KOH is used to convert it to potassium stearate. The weight ratio of stearic acid to polyethylene wax is preferably in the range of from 1:5 to 1:6, though this may be varied some. Potassium hydroxide is used in an amount sufficient to convert the stearic acid to potassium stearate and to produce a pH of at least 9, preferably of from 9 to 12, in the final emulsion.