Background of the Invention
Metal has been used to enhance the burning rate of solid propellant compositions. The metal has been added to uncured solid propellant compositions in various forms, e.g., ribbons, powder, staples, spheroidal, and other geometric shapes.
More recently, U.S. Pat. No. 4,092,189 issued to Robert E. Betts on May 30, 1978 and assigned to the United States of America as represented by the Secretary of the Army, Washington, D.C., is directed to a method of preparing high burning rate solid propellant grains that have good mechanical properties. This patent covers a high burning rate solid propellant grain prepared from a multimodal blend of at least one ultra-high burning rate propellant that has been cured and ground to a predetermined particle size of from about 100 microns (0.1 millimeter) to about 5 millimeters and at least one uncured propellant composition that has high tensile strength and compatibility with the ultra-high burning rate propellant and that serves as a binder for the solid propellant grain when cured.
The method of U.S. Pat. No. 4,092,189 includes preparing a cured ultra-high burning rate propellant that is subsequently ground and screened to a predetermined particle size. The ground and screened propellant is then combined with uncured propellant that is subsequently cured to yield a high burning rate solid propellant grain with good mechanical properties.
An improvement to the burning rate technology provided by an improved process in producing the enhancer for propellant burning rate and the technique of using the enhancer for propellant burning rate would be welcomed additions to the propulsion industry art.
Therefore, it is an object of this invention to provide a means for effecting a major increase in the burning rate of solid propellants.
Another object of this invention is to provide burning rate enhancement of solid propellants by means of metal/oxidant agglomerates.
A further object of this invention is to provide metal/oxidant agglomerates which are prepared by an improved method wherein the agglomerates formulation is slurred in a fluorinated and/or chlorinated hydrocarbon solvent at ambient temperature to form agglomerates in mixture, followed by maintaining the mixture at 135 degrees Fahrenheit with stirring, and with continued stirring while the mixture is maintained under reduced pressure to remove any residual solvent. Subsequent curing of the agglomerates is accomplished at 150-170 degrees Fahrenheit for about 24 hours.
Summary of the Invention
The metal/oxidant agglomerates of this invention which provide a means of burning rate enhancement of solid propellants are produced from a finely divided metal selected from aluminum, boron, and titanium, ammonium perchlorate, and a small quantity of the same binder material that goes into the manufacture of the propellant, such as, hydroxyl-terminated polybutadiene crosslinked with a polyisocyanate. Additional ingredients can be incorporated into the metal/oxidant agglomerates to bring about further enhancement of burning rate. These additional ingredients can include one or more ingredients selected from an ammonium perchlorate decomposition accelerator (0.2-0.5 weight percent) (e.g., triphenylbismuthine), a carboranyl burning rate enhancer (0.5-2.0 weight percent) (e.g., n-hexylcarborane), iron oxide (0.1-2.0 weight percent), etc. These additives can be used in varied ratio, e.g., triphenylbismuthine 0.5%, n-hexylcarborane 0.5%, and iron oxide 1.0% or the additive can be used alone in the agglomerate formulation.
The method of preparing the metal/oxidant agglomerates for use in this invention is summarized as follows: The various ingredients, consisting of the finely divided metal, ammonium perchlorate, hydroxyl-terminated polybutadiene, isophorone diisocyanate, the ammonium perchlorate decomposition accelerator, and a burning rate enhancer are slurried in Freon TF (trichlorotrifluoroethane) for 15 minutes at ambient temperature to form agglomerates, followed by increasing temperature to about 135 degrees Fahrenheit and maintaining the mixture at 135 degrees Fahrenheit with stirring for final agglomerate formation, followed by maintaining under reduced pressure to remove any residual Freon, and then followed by curing the agglomerates at 150-170 degrees Fahrenheit for about 24 hours.
The agglomerates are screened to separate the agglomerates into different mesh sizes. The most effective mesh size is in the range of 300-500 micrometers. The agglomerates are incorporated into an uncured propellant formulation in percentages of the order of 1-5%. The higher the amount of agglomerate the higher will the burning rate enhancement be. A typical baseline propellant to which the agglomerates are incorporated contains a high solid loading of a blend of fine and ultrafine ammonium perchlorate, aluminum metal fuel, hydroxyl-terminated polybutadiene, diisocyanate crosslinking agent, and metal oxide burning rate catalyst. For higher catalytic performance a carboranyl burning rate catalyst can be employed. Additionally, a perchlorate decomposition accelerator, triphenylbismuthine can be used.
Description of the Preferred Embodiment
Preformed agglomerates are prepared from a metal (aluminum, boron, titanium, etc.), ammonium perchlorate, and a small quantity of the same binder material that goes into the manufacture of the propellant, e.g., hydroxyl-terminated polybutadiene crosslinked with a polyisocyanate. Optimum mesh size of the agglomerates is 300-500 micrometers. The agglomerates cause a major increase in the burning rate of solid propellants when incorporated therein in the percentages of 1-5%.
A preferred procedure for preparing the agglomerates is as follows: The various ingredients, as set forth in Table I below: Composition of a Typical Agglomerate, are slurried in a fluorinated and/or chlorinated solvent (e.g., trichlorotrifluoroethane or trichloroethylene) for 15 minutes at ambient temperature. The slurried mixture is maintained at about 135 degrees Fahrenheit with stirring for final agglomerate formation. Finally, the stirring is continued under reduced pressure to remove any residual solvent. The agglomerates are then cured at 150-170 degrees Fahrenheit for 24 hours.
The type solvent selected for use in the formation of the agglomerates should be a solvent in which the agglomerate formulation ingredients are insoluble and one which can be readily removed under reduced pressure. In addition to Freon TF, other fluorinated and/or chlorinated hydrocarbon solvents, such as trichloroethylene, can be used in the method wherein agglomerates are formed in the slurried mixture. The formation technique will result in a range of particle sizes for the agglomerates formed; therefore, for more precise control of the end results, screening of particle size or sizes for optimum results can be made for a desired level of performance and burning rate enhancement.
The composition of a typical baseline propellant used in the evaluation of the effectiveness of agglomerates as a means of burning rate enhancement is presented in Table 2 below.
The new concept of this invention has the potential of producing solid propellants which have burning rates in the 20-30 inches per second regime at 2000 psi operating pressure. Since this concept requires only the usual propellant ingredients, rather than undeveloped or expensive constituents, it represents a breakthrough in the development of ultrahigh burning rate, solid propellants. Using this approach, it should be possible to attain burning rates heretofore unattainable.