The present invention pertains generally to the destruction of munitions or other devices containing enclosed energetic materials. In particular, the present invention pertains to the destruction of such materials via hydrolysis. The present invention is particularly, but not exclusively, useful as a system and method for chemically disposing energetic materials enclosed in assembled devices without pretreatment of the assembled devices.
Destruction of devices containing energetic materials such as explosives, munitions and propellants is a hazardous operation. Often, energetic materials are mechanically removed from these devices. For instance, such materials may be removed by “autoclave melting out” or “steaming out.” However, these processes cannot be used for energetic materials having high melting points, or those energetic materials which ignite before they melt. Another mechanical process used to remove energetic materials is fluid washout by cavitating or non-cavitating high pressure jets. The cavitating jet process involves the impact of vapor bubbles on the devices and may create uncontrolled reactions in the energetic material. Further, non-cavitating fluid jets typically do not operate at pressures that are adequate for efficient erosion of the energetic material. In addition, both of the jet processes use extensive amounts of water, which may be undesirable in certain environments. In other instances, the energetic material may be disposed of by open burning, open detonation, or incineration. However, such methods are not preferred due to the resulting pollution.
While these and other methods are generally effective, they do not obviate the danger involved in mechanically operating on devices encapsulating energetic material. In light of the above, it is an object of the present invention to provide a system and method for chemically disposing energetic material enclosed in assembled devices. Another object of the present invention is to provide a system and method for disposing energetic material enclosed in assembled devices with minimal pretreatment of the devices and without detonating or igniting the energetic material. Another object of the present invention is to provide a system and method for disposing energetic material enclosed in assembled devices without mechanically operating on the devices. Another object of the present invention is to provide a system and method for disposing of energetic materials enclosed in assembled devices in which the assembled devices are chemically penetrated to allow access to the energetic material. Still another object of the present invention is to provide a system and method for disposing of energetic materials in assembled devices in which the energetic material is exposed only within a hydrolysis solution. Yet another object of the present invention is to provide a system for disposing energetic material enclosed in assembled devices which is simple to operate, relatively easy to manufacture, and comparatively cost effective.
In accordance with the present invention, a system for chemically disposing energetic material enclosed in assembled devices comprises a porous basket for receiving the devices. For the present invention, the basket is connected to a basket arm for rotation about a basket axis. Further, the basket is connected to a lifting arm for moving the basket into and out of a tank holding a caustic or acidic hydrolysis solution. For the present invention, the basket is submerged in the hydrolysis solution by the lifting arm and is rotated therein by the basket arm. Preferably, a caustic hydrolysis solution is between approximately 60° C. and approximately 130° C. and between about 4 wt. % and about 50 wt. % sodium hydroxide. Further, an acidic hydrolysis solution is preferably between approximately 50° C. and approximately 80° C. and between about 3M and about 8M nitric acid.
Upon submersion of the devices in the hydrolysis solution, the solution flows into contact with the assembled devices to facilitate a reaction. During the reaction between the assembled devices and the hydrolysis solution, the assembled devices are penetrated by the hydrolysis solution. As a result, the hydrolysis solution contacts and reacts with the energetic material to render the energetic material non-energetic.
For the present invention, the system further includes a rinse fluid housed in a container. In order to use the rinse fluid, the lifting arm is adapted to remove the basket from the hydrolysis solution after the energetic material is rendered non-energetic, and to immerse the basket in the rinse fluid. Similar to its use with the hydrolysis solution, the basket arm is adapted to revolve the basket in the rinse fluid to rinse off components remaining in the basket.
As an additional component, the system includes a heat exchanger for selectively adding and removing heat from the hydrolysis solution. By modulating the temperature of the solution with the heat exchanger, the reaction rate can be controlled. Alternatively, or additionally, the solution temperature and reaction rate may be controlled by selectively adjusting the surface area of the solution. Specifically, the system includes surface objects, such as floats, that may be positioned on or removed from the surface of the solution. As a result, the exposed surface area of the solution is selectively increased or decreased. In this manner, the evaporation rate and temperature of the solution are controlled.
For purposes of the present invention, the system also includes an exhaust hood for capturing hydrogen or other gases that are released during the hydrolysis process. In order to prevent a build up of the gases to explosive levels, the system is provided with a diluting device that mixes air into the gases to dilute them to non-explosive concentrations. Further, the exhaust hood is provided with an exhaust vent to eliminate gases from the hood.
The novel features of this invention, as well as the invention itself, both as to its structure and its operation, will be best understood from the accompanying drawings, taken in conjunction with the accompanying description, in which similar reference characters refer to similar parts, and in which:
Referring initially to
For the purposes of the present invention, it is important to keep the basket 16 completely submerged to maintain the continual moderating effect of the solution 14. If a portion of the basket 16 emerges from the solution 14 during the reaction of the devices 26, then energetic material 27 can adhere to the wall of the tank 12 or otherwise be pulled out of the solution 14. Without the moderating effect of the solution 14, the heat of the hydrolysis reaction can ignite or detonate the unreacted energetic material 27.
For a caustic hydrolysis solution 14, the solution 14 preferably contains between approximately 4-50 wt. % sodium hydroxide. Preferably, a solution 14 containing sodium hydroxide is kept between approximately 60-130° C. For an acidic hydrolysis solution 14, the solution 14 preferably contains between about 3M and about 5M nitric acid and is kept between approximately 50-80° C. While sodium hydroxide and nitric acid are expressly disclosed herein, other bases or acids could be used.
In order to keep the solution 14 at a desired temperature, the system 10 is provided with a controller 28 and a heat exchanger 30. Specifically, the controller 28 is able to monitor the temperature of the solution 14 and to operate the heat exchanger 30 to increase or decrease the temperature as needed. Additionally or alternatively, the temperature of the solution 14 may be controlled by manipulating the exposed surface area of the solution 14. As shown in
When the solution 14 evaporates from the surface 32 it is captured by an exhaust hood 36 that is positioned over the tank 12. In order to recycle the solution 14 that evaporates from the surface 32, the system 10 is provided with a condensation device 38 that condenses the solution 14 in vapor form, and returns the condensed solution 14 back to the tank 12 via a condensation return 40. For the present invention, the exhaust hood 36 also captures hydrogen and/or other gases released as a result of reactions within the solution 14. In order to prevent a build up of these gases to explosive levels, the system 10 is provided with a diluting device 42 that mixes air into the gases to dilute them to non-explosive concentrations. Also, condensable components of the gases, such as water, may be condensed and returned to the solution 14 via the condensation return 40. Further, the exhaust hood 36 is provided with an exhaust vent 44 to provide for the elimination of gases.
As stated above, the basket arm 20 is provided to rotate the basket 16 in the solution 14. Operationally, the basket 16 and basket arm 20 are rotated by a rotation mechanism 46. If the basket 16 were not rotated, gas produced during reactions in the solution 14 would form in pockets around the devices 26. As a result, the pockets would prevent the solution 14 from contacting all of the material to be hydrolyzed and could potentially lead to explosive gas mixtures within the solution 14. Further, without basket rotation, the reactants in the solution 14 may be depleted locally around material to be hydrolyzed. However, rotation of the basket ensures that no local depletion in the solution 14 occurs. For the present invention, the basket 16 is rotated until all of the energetic material 27 is rendered non-energetic.
As further shown in
For the present invention, the system 10 further provides for post-reaction treatment of the components remaining in the basket 16, i.e., the materials not reactive to the solution 14. Specifically, the system 10 includes a rinse fluid 60 that is held within a container 62. Further, the lifting arm 18 is adapted to remove the basket 16 from the tank 12 and to immerse the basket 16 in the rinse fluid 60. As during the reaction process, the basket arm 20 is able to rotate or revolve the basket 16 within the rinse fluid 60 to rinse off the non-reactive components remaining in the basket 16. After the components are thoroughly rinsed, the basket 16 is withdrawn from the rinse fluid 60 and is unloaded.
As shown in
Referring now to
Complete submersion of the basket ensures that the solution maintains its moderating effect on the energetic material. If the basket or tank emerges from the solution before the energetic material is rendered non-energetic, the heat of hydrolysis can ignite or detonate the energetic material. Further, if the energetic material emerges from the solution, it may adhere to the tank or another device component. After it is submerged, the basket is rotated in the solution to facilitate a reaction between the assembled devices and the caustic hydrolysis solution. For the present invention, rotation of the basket prevents the formation of pockets of gas on the devices and ensures that all surfaces of the devices are contacted with the caustic solution (action block 104).
While the basket is submerged and rotated, the reaction rate between the device, energetic material and caustic solution is controlled (action block 106). Specifically, the reaction rate may be controlled by manipulating the temperature of the solution by selectively adding heat thereto or removing heat therefrom. Alternatively or additionally, the reaction rate may be controlled by selectively increasing and decreasing the surface area of the caustic hydrolysis solution to control the temperature of the solution. For either method, the caustic hydrolysis solution is preferably kept between approximately 60° C. and approximately 130° C.
As shown in action block 108, the method further includes the step of mixing the solution. In practice, the solution may be mixed by a mechanical agitator in the tank, by forcing fluid into the tank via jets, or by recirculating the solution through the tank.
When the energetic material has fully reacted and is rendered non-energetic, the basket is removed from the solution (action block 110) by the lifting arm. The lifting arm then immerses the basket in the rinse fluid (action block 112). While in the rinse fluid, the basket is revolved in order to rinse off any components remaining in the basket (action block 114). Thereafter, the basket is withdrawn from the rinse fluid (action block 116) and any remaining components are unloaded from the basket (action block 118). The remaining components, such as unreacted non-energetic remnants of the devices may be recovered and recycled.
As further shown in
While the particular Hydrolysis System and Process for Devices Containing Energetic Material as herein shown and disclosed in detail is fully capable of obtaining the objects and providing the advantages herein before stated, it is to be understood that it is merely illustrative of the presently preferred embodiments of the invention and that no limitations are intended to the details of construction or design herein shown other than as described in the appended claims.
The U.S. Government has a paid-up license in this invention and the right in limited circumstances to require the patent owner to license others on reasonable terms as provided for by the terms of Contract No. F08630-02-C-0083 awarded by the United States Air Force.
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Number | Date | Country | |
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20080086024 A1 | Apr 2008 | US |