1. Field of the Invention
The invention relates to an insenstive, pressable and castable explosive and a process for the production of said explosive.
2. Discussion of the Prior Art
The invention is based on a phlegmatised explosive, corresponding to EP 0 509 200 B1 and DE 40 06 961. This involves explosive mixtures in which the particulate explosive is coated with a phlegmatising inert binder. Improved insensitivity is achieved with those binders. In the meantime the demands in respect of insensitivity have been set at a markedly higher level. Those demands are not attained by the known binders.
The object of the invention is to propose a high-energy, insensitive pressable explosive.
The invention attains that object in providing an explosive which comprises:
The invention advantageously provides that an at least monomolecular layer is applied to the crystals of the explosive and fills surface flaws. That eliminates very fine pores which otherwise act as so-called hot spots, with the effect that the explosive reacts in an unwanted fashion when subjected to a relatively low level of loading. The complete wetting effect provides that a high-energy explosive already achieves virtually a 100% theoretical density with just a low inert proportion. As a result, because of the virtually zero porosity of the explosive charge, this affords a further enhanced level of insensitivity with an increased degree of efficiency. This explosive is suitable for shaped charges and fragmentation charges.
An explosive having the following composition:
There are three suitable alkyl polysiloxanes, namely
dimethyl polysiloxanes
methyl hydrogen polysiloxanes, and
methylphenyl polysiloxanes.
1. The production process comprises the following steps:
Octogen in an amount of 70 parts of coarse grain is mixed with 30 parts of fine grain in a container.
2. A polyalkylsiloxane solution is diluted with isopropanol in a ratio by volume of 1:6, added to the explosive mixture and stirred until complete wetting has taken place.
3. The mixture is dried.
4. In a suction filtration apparatus the slurry is washed 3 to 4 times with distilled water and sucked away as far as possible.
5. The mixture is dried.
6. In parallel therewith a solution is made up from 1 part of Hy Temp and 3 parts of DOA in 25 parts of solvent mixture comprising 60% ethanol, 20% acetic acid ethyl ester and 20% acetone.
7. The dried, pretreated explosive mixture is added to the prepared binder solution in a Drais mixer and mixed at 40° C. for about 1-2 hours with same at a medium agitation speed (rotary speed 60/min).
8. The solvent is completely removed with continuing agitation under a pump vacuum, duration about 2 to 3 hours, wherein finally a dry pressable granular material with an approximately 1 to 2 mm particle diameter is produced.
The production process is to be carried out in an equivalent fashion, on the basis of hexogen.
Number | Date | Country | Kind |
---|---|---|---|
101 55 885 | Nov 2001 | DE | national |
Number | Name | Date | Kind |
---|---|---|---|
2102372 | Mills | Dec 1937 | A |
3984264 | Lampert | Oct 1976 | A |
4794180 | Heinemeyer et al. | Dec 1988 | A |
5183520 | Wanninger et al. | Feb 1993 | A |
5547527 | Muller et al. | Aug 1996 | A |
5750921 | Chan et al. | May 1998 | A |
Number | Date | Country |
---|---|---|
40 06 961 | Sep 1991 | DE |
41 26 981 | Jan 1993 | DE |
197 19 073 | Nov 1998 | DE |
509 200 | Oct 1992 | EP |
Number | Date | Country | |
---|---|---|---|
20030127166 A1 | Jul 2003 | US |