A METHOD OF PHLEGMATIZATION OF CRYSTALLINE EXPLOSIVES AND OTHER EXPLOSIVE CRYSTALLINE SUBSTANCES, AS WELL AS A METHOD OF PRODUCING PLASTIC BOUND EXPLOSIVES AND SUBSTANCES PRODUCED ACCORDING TO THE METHOD

Abstract: The disclosure primarily relates to a method of phlegmatizing crystalline or otherwise particulate explosive substances or compositions in which these are included, by first coating the discrete particles with a thin layer of oxazolin wax in order thereafter to carry out a conventional wet-granulation with a true phlegmatization agent or a binder agent, such as one of the wax types included under different explosive standards or a plastic composition. The invention also concern products manufactured according to said method.

Description: TECHNICAL FIELD The present invention relates to a method of phlegmatization (also known as desensitization) of crystalline explosives such as octogen, hexogen, PETN and other crystalline or particulate explosive substances and compositions in which such explosives or explosive substances are included. The invention further relates to a method of producing a preproduct for the production of plastic bound explosives (generally abbreviated PBX) according to methods known per se. The invention finally also relates to substances produced according to said methods. Background art Octonal and hexotonal are examples of phlegmatized compositions which may be manufactured according to the invention. These compositions normally include, respectively, octogen or hexogen, TNT, powdered aluminium and a phlegmatization agent, usually in the form of wax. There are military standards for octogen and hexogen which standards require these substances to be phlegmatized with one of a number of waxes of defined quality. The most common is petroleum wax, but also acid wax, ester wax or their combinations are frequently used. The phlegmatization of octogen, hexogen and PETN crystals by a granulation process and coating them with a fusible substance such as a wax or the like is necessary if one wants to melt such crystalline explosives or to compact them to form unitary blasting charges or explosive devices. In such an event the phlegmatization agent serves as a binder and, in the compaction process, also as a lubricant. Plastic bound explosives or PBX also consist of crystalline or particulate explosive substances such as hexogen, octogen or PETN which are agglutinated with a suitable plastic binder and fused to the desired charge sizes and configurations by compaction with a possible application of heat. As examples of plastic binders for PBX, Nylon® and polystyrene may be mentioned. Particulate, non-explosive substances such as powdered aluminium or graphite may also be included in PBX. The plastic bonded explosives (PBX) are produced by adding a solution or dispersion of plastic to an aqueous slurry or dispersion of the crystalline or particulate explosive. The solvent or dispersion agent in which the explosive was dissolved or dispersed is subsequently being removed which causes the deposition of the plastic binder on the explosive crystals or particles. As a rule, the coating with plastic also results in a certain granulation, since the discrete crystals or particles are being bound to form granules. These plastic-coated granules may then be shaped by compaction and heating into blasting charges or explosive devices of the desired size and shape. It is also known in the art to flegmatize crystalline or particulate explosive substances such as hexogen or octogene with wax added by the aid of a solvent according to same type of general method as already described for the plastic binders. The wax is thus thereby added to a suspension of the explosive substance in an inert fluid, e g consisting of water, dissolved in a solvent which is driven off under continous agitation thereby causing the wax to deposit on the particulate explosive particles. As it has been mentioned above, there are military specifications which require the phlegmatization of octogen and hexogen, even in bulk form, with a wax which meets certain standards. There is a plurality of wax types employed for this purpose, of which mention might be made of Wax Composition 1 and D2, but other wax types may also be considered. Normally, the phlegmatization of octogen and hexogen is carried out by wet granulation in water. In this process an amount of wax is added to the aqueous bath whose temperature is raised to a point at which all wax is melted; subsequently, the temperature of the water is gradually decreased so that the wax is deposited on the explosive crystals. Uniform distribution of the phlegmatization agent over the crystals is obtained by suitable agitation and temperature regulation of the granulation suspension. It is also possible, to some degree, to control by these means the size of the granules so obtained. The state of the art concerning the two methods described above for the addition of a wax to a crystalline or explosive substance suspended in an inert solvent such as water by the aid of either heat and a gradually increasing temperature or by the aid of a solvent which is gradually driven off are both exemplified in FR-A-1,602,624. However, it is generally known to persons skilled in the art that it is difficult to produce uniform, evenly phlegmatized granules of explosives. This is due to the fact that the wax does not spread sufficiently uniformly on the crystal surfaces and shows a tendency to form large and small flocks with the particulate substances. The flocculation tendencies of the wax become particularly troublesome in the production of octonal and hexotonal in which case the wax causes flocculation of the powdered aluminium constituting a component of these composite explosives. The same problems occur in the manufacturing of preproducts for the production of PBX. Many of the plastics, including the generally employed Nylon®, which are otherwise excellent PBX's binders, display a poor adhesion to the explosive crystals. A considerable proportion of the crystals may therefore remain uncoated, while the plastic, together with remaining explosive crystals form large aggregates with a high concentration of plastic. We have now found a method which reduces these problems to a considerable degree, when applied to production of phlegmatized crystalline explosives and preproducts for the production of PBX. According to the present invention, the explosive crystals are initially coated with an oxazolin wax and subsequently coated by the phlegmatization agent proper or a suitable plastic binder. Oxazolin wax is a double unsaturated heterocyclic compound extracted from nitroparaffins. It has a melting point of 160°C and a molecular weight of about 1352. It is commercially available under the name of Oxazolin wax TX2®. Oxazolin wax as an additive to explosive substances is known per se through US-A-3 438 823. According to said patent the oxazolin wax however is used as a wetting agent to render a first water soluble particulate explosive component, such as ammonium nitrate, wettable by a second liquid explosive sensitizing ingredient such as nitrocellulose. Said US patent thus describes a different product and process. The amount of initially added oxazolin wax according to the invention may vary, but should be sufficient to coat the discrete crystals. The oxazolin wax is added in an introductory wet granulation stage to crystalline explosive suspended in the mixing water, possibly together with similarly suspended solid particulate substances as powdered aluminium or the like. The oxazolin wax is dissolved in a suitable solvent such as trichloroethane or Chlorothene®. Subsequently the temperature of the mixing water is raised, under agitation, to or slightly above the boiling point of the solvent and is held constant until the solvent has been evaporated; during the evaporation the oxazolin wax is gradually deposited on the solid particles. Then the phlegmatization agent such as for example, Wax Composition 1 or type D2 is added. As a rule, a further temperature increase is then required for melting the phlegmatization agent. Subsequently the temperature of the mixing water, under suitable agitation, is progressively reduced to enable deposition of the phlegmatization agent on the oxazolin wax. Such a pretreatment with oxazolin wax has proved to facilitate the phlegmatization process and to give a more uniform granulation, suppressing at the same time the above-mentioned flocculation tendencies. This applies to both the pure granulated explosives and to composite products of the hexotonal and octonal type. We also found that it is possible to produce an excellent starting material for PBX in the form of uniformly plastic-coated explosive granules if the explosive crystals or particles are first coated with a thin layer of oxazolin wax and the oxazolin wax-coated particles are then coated and granulated with the plastic binder as considered herein. The explanation for this is that the oxazolin wax has proved to be an excellent basis for further coating with some of the plastics which may come into consideration as binders in PBX. According to the present invention, oxazolin wax dissolved in a suitable solvent such as 1,1,1-trichloroethane or Chlorothene® (methyl chloroform) is added to the water-dispersed explosive particles and, thereafter, the solvent is successively removed under continuous agitation and temperature regulation of the suspension, so that the oxazolln wax is caused to deposit evenly over the explosive particles. When the explosive particles have been coated in this manner, with a thin layer of oxazolin wax covering them substantially totally, the plastic binder is added, dissolved or dispersed in a specifically intended solvent or dispersion agent. This latter is removed or driven off under agitation and temperature regulation of the dispersion, which causes the plastic binder to deposit on the previously obtained oxazolin wax layer. In this manner, an excellent PBX is obtained consisting of granules of uniform size which are completely coated with plastic layers of even thickness. According to the present invention the plastic solution or dispersion may be added dropwise to the explosive's dispersion which has a temperature higher than the boiling point of the solvent or dispersion agent of the plastic so that the solvent or dispersion agent evaporates more or less instantaneously. Alternatively, the entire batch of plastic may be added to the cold explosive's dispersion and the temperature thereof is subsequently elevated to evaporate the solvent or dispersion agent of the plastic. The method according to the present invention has been defined in the appended claims, and will now be described in greater detail in conjunction with the following non-restrictive Examples. As defined in the claims the method according to the invention also makes it possible to produce phlegmatized, crystalline or particulate explosive or other explosive crystalline and/or particulate substance or composition in which such a crystalline and/or particulate explosive or explosive substance is included in which crystals and/or other solid particles included therein are coated with a thin inner layer of oxazolin wax which, in its turn, is surrounded by an outer totally superposed layer of phlegmatization agent, for example, in the form of a wax or a plastic composition. EXAMPLE 1 Method of Producing Phlegmatized Octogen. 150 litres of water and 47.5 kg of octogen (with a particle diameter of 170 µm) particle size of between 100 and 300 µm) and 0.04 % of oxazolin wax TX2 dissolved in chlorothene (the amount of oxazolin wax based on the amount of explosives) were added to a reaction vessel equipped with a mechanical agitator and provided with a heat exchanger for heating and cooling. The water temperature was gradually raised to 95°C and during this time the chlorothene was driven off and the oxazolin wax was deposited on the crystalline explosive. When the chlorothene has been driven off and the contemplated temperature has been attained, 2.5 kg of the phlegmatization wax (Wax Composition 1) was added, the content of the reactor was kept at a constant temperature for 10 minutes, cooled and Nutsch-filtered. This resulted in a homogeneous product with the phlegmatization wax evenly and uniformly distributed over the crystal surfaces. The particle size distribution of the product so obtained was narrower than those which could have been expected for a product obtained without deposition of oxazolin wax. The employment of oxazolin wax results in a more uniform distribution of the phlegmatization agent over the particles and thereby helps to avoid the formation of coarse particles which consist mainly of the wax alone. The even and uniform phlegmatization is especially important if the product is to be compressed to a compact body, as, for example, in the production of initiators, primary explosives and the like. In this case, the mean size of the obtained particles was approx 350 µm. EXAMPLES 2 AND 3 Method of Producing Phlegmatized Hexogen and PETN. Experiments corresponding to the experiment of Example 1 have been carried out with hexogen and PETN resulting in essentially the same average particle size and the same properties of the final products. EXAMPLE 4 Method of Producing PBX. The following process has been employed for the production of the plastic bonded explosive (PBX) PBX-MIL Spec. Type A, containing 8.5 % polystyrene (PS), 1.5 % diocthylphthalate (DOP) and 90.0 % hexogen. To 90 g of hexogen (mean particle diameter approximately 100 µm) slurried in 500 ml of water 1.5 ml of oxazolin solution (15 g/l in chlorothene) is added and the mixture is heated to 90°C. A solution of 8.5 g of PS, and 1.5 g of DOP, in 50 g of methylethylketone is added and the solvent is distilled off. The batch is cooled and the product is filtered-off and dried. The result is an excellently granulated PBX, which fully satisfies the military standard MIL-P 14999. EXAMPLE 5 Method of Producing PBX. The following process, similar to that disclosed in Example 1, has been employed to produce PBXN-2, a PBX containing 5.3 % of Elvamid 8061 (a Nylon) and 94.7 % of octogen. 94.7 g of octogen (mean particle diameter 50-100 µm) is slurried in 500 ml of water and 1.5 ml of oxazolin solution is added. The batch is heated to 90°C, 5.3 g of Elvamid dissolved in 50 ml of methanol is added, and the heating is continued to 95°C to drive off the solvent. After cooling, filtering and drying, a product with a mean particle diameter of approx. 0.5-1,0 mm is obtained. EXAMPLE 6 Method of Producing PBX. The process disclosed in Example 5 was repeated, substituting octogen with hexogen (66 %, mean particle diameter approx. 100 µm) and powdered aluminium (25 %), and increasing the content of the Elvamid to 9 %. The granules of a mean particle diameter of approx. 0.5-1.0 mm, fully satisfying the requirements as laid down according to NAVORD Syst. Command OS11632A have been obtained.

Claims: A method for the phlegmatization of crystalline explosive substances such as octogen, hexogen and PETN, or a method for the production of preproducts for the production of plastic bound explosives (PBX), or combinations in which such explosive substances are included together with one or more other solid, particulate but non-explosive substances such as powdered aluminium or the like, by wet granulation with a phlegmatization or binder agent of a type known per se, for example in the form of a wax or a plastic binder, in water, characterized in that a minor portion of said phlegmatization or binder agent is substituted by oxazolin wax which is initially batched to the granulation suspension (the solid particulate substances suspended in water), dissolved in a solvent such as 1,1,1-trichloroethane, whereafter the solvent is driven-off under continuous agitation of the granulation suspension such that the oxazolin wax is caused to deposit on the particle surfaces before the phlegmatization agent (the wax) proper or the binder agent (the plastic material) is added, and, in its turn, during continued and continuous agitation and temperature regulation of the suspension, is caused to deposit on the oxaxolin wax and to provide thereon a total covering and a suitable granulation of the particles. The method as claimed in claim 1, characterized in that the oxazolin wax is added in an amount corresponding to from 0.01 to 0.1 weight per cent, calculated on solid particulate substance. A phlegmatized, crystalline or particulate explosive or other explosive crystalline and/or particulate substance or composition in which such a crystalline and/or particulate explosive or explosive substance is included, produced according to the method as claimed in claim 1 or 2, characterized in that crystals and/or other solid particles included therein are coated with a thin inner layer of oxazolin wax which, in its turn, is surrounded by an outer totally superposed layer of a phlegmatization agent, for example, in the form of a wax or a plastic composition.

Inventors: BACK, SIGURD, ERICSSON, PER, NYQVIST, JAN-OLOF
Applicants: NOBEL KEMI AB
Application year: 1986
Main classification: C06B21
IPC codes: C06B45, C06B21, C06B23