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Publication numberUS2852360 A
Publication typeGrant
Publication dateSep 16, 1958
Filing dateMar 13, 1956
Priority dateMar 16, 1955
Publication numberUS 2852360 A, US 2852360A, US-A-2852360, US2852360 A, US2852360A
InventorsBy Nils Gustav
Original AssigneeBofers Ab
Export CitationBiBTeX, EndNote, RefMan
External Links: USPTO, USPTO Assignment, Espacenet
Method of manufacturing explosives
US 2852360 A
Abstract  available in
Previous page
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Claims  available in
Description  (OCR text may contain errors)

Sept. 16, 1958 N. G. BY

METHOD OF MANUFACTURING EXPLOSIVES Y wzjooo R B H m V m A V mo-2am oP a @2308 W. U G S l N BYMAALAI'."(Ida,K

wz oou ME; 600 H Filed March 13, 1956 iinited States was METHOD 01F MANUFACTURING EXPLOSTVES Nils Gustav By, Karislkoga, Sweden, assignor to Airtiebolaget Bofers, Bofers, Sweden, a Swedish corporation Application March 13, 1956, Serial No. 571,236 Claims priority, application Sweden March 16, 1955 4 Claims. (Cl. 52-20) This invention relates to explosives; and in particular, is directed to a novel process for the manufacture of granulated mixed explosives containing trinitrotoluol.

It is known to manufacture mixed explosives containing TNT (trinitrotoluol) in such way that the explosives other than the TNT, as for example, cyclotrimethylenetrinitramine (cyclonite RDX), methylnitramine (tetryl), pentaerythritol tetranitrate (PETN), ammonium picrate (explosive D), aluminum, etc. are added to the molten TNT and distributed in the molten TNT by stirring. The mixed explosive thus produced is thereafter subjected to generally known operations for the manufacture of granules, flakes or cakes. It is thus possible to manufacture mixed explosives containing TNT where the explosives are directly brought together. By such manufacture, the mixture will constitute one single coherent unit, whereby the mutual relation between the ingredients can be varied to a very great extent. The most serious disadvantage of this method of manufacturing mixed explosives is the hazard of accidents due to fires or explosions caused by the necessity of working with a considerable coherent quantity of the explosives at one time during the mixing operation.

In order to lessen such hazard of explosion, it is possible to carry out mixing of the explosives in a solution, preferably of water. In the water, the mixed explosives will be produced in the form of grains, which are not in contact with each other. According to this last mentioned method, the mixing is carried out in one step. The disadvantage of the last mentioned method is that the relation between the explosive ingredients in the mixture can only be varied to a very small extent. Thus, the TNT content in the mixed explosive lies between 5% and 20%. Where attempts are made to manufacture mixed explosives by carrying out the intermixing in water, and using TNT in quantities outside the aforesaid range of from 5 to 20 percent, it is found that when the mixed explosive stiifens, granules are obtained but the grains can differ from each other considerably both in composition and size. When the TNT content thereof is comparatively small, very different sizes of grains and crystals are obtained. If the TNT content is high, it is difficult to maintain good distribution in the aqueous phase, and when the mixture cools, a part thereof stiifens and forms a firm cake. It is only when the TNT content is of such an optimum value in the suspension described above that a final result can be achieved wherein the granules exhibit evenness of grain size combined with homogeneity of composition without the separation therefrom of a firm cake of TNT.

According to the present invention, by using two steps, it is possible to vary the mutual relation between the explosive ingredients to the same extent as is possible in the method where the ingredients are mixed directly with each other. Accordingly, it is among the principal objects of the present invention to provide a process to govern the manufacture of granules of mixed explosives pontaining varying quantities of TNT in such a way 2,4,6-trinitrophenyl- Patented Sept. 16, 195% that the product produced will be granules with evenness of composition and grain size.

I have found that such objective is attained if the manufacture be divided into two separate steps, which may appropriately be designated as the primary and the secondary granulation. When the manufacture is carried out in batches, the primary and secondary granulation may be carried out seriatim in the same vessel. The method may easily be adapted or converted to a continuous operation in which different vessels are used for the primary and secondary granulations. To carry out the primary granulation, a watery suspension of molten TNT is made with such a quantity of the TNT that in each individual case, together with the other component explosives, granules of even or uniform composition and grain size may be obtained. The additional portion of TNT desired to bring the TNT content of the final granules to a desired value is introduced in the subsequent secondary granulation. If a correctly proportioned quantity of TNT be used, granules of the mixed explosive will be produced in the first operation that are characterized by great homogeneity of composition, have an appropriate grain size and are devoid of any tendency to stick together or collect on the walls of the apparatus.

in carrying out the secondary granulation, the granules produced in the primary granulation, together with the mother liquid or together with some other suitable suspending liquid as for example alcohol and/or glycerine is used to which there is added the remaining portion of the TNT in molten condition. This addition can be accomplished by means of an appropriate sprinkling device. While the mass is vigorously stirred, if a correct temperature has been chosen, the TNT will precipitate on the primary granules. it is of great importance that an appropriate temperature be used in the last-mentioned operation. The temperature depends upon the type of mixed explosives (as for example, cyclotol: 60% cyclonite and 40% TNT, tetrytol: 70% tetryl and 30% TNT, pentolite: 50% PETN and 50% TNT, picratol: 50% explosive D and 50% TNT), i. e. on the composition and on the granulating conditions, as for example the form or shape of the vessel and/or the stirring conditions. The temperature is determined empirically in each individual case by a laboratory test; and then this temperature is applied to the full scale operation. Generally the temperature should lie in the approximate range of 70 to C. If the temperature be too high, there is a hazard that a sticky material will be produced. If the temperature be too low, the granules produced will not be even and homogeneous.

The following are illustrative examples of mixed explosives made in accordance with this invention; and the accompanying drawing shows a general organization of apparatus suitable for carrying out such manufacture.

Example 1 Manufacture in batches of granulated mixed explosive containing about 40% TNT While stirring well mix at approximately C. 1 weight portion RDX, 0.18 part TNT, 3.3 parts water, 0.02 part wax, as for example, beeswax, Canada Wax or carbowax, and a little wetting agent, as for example, a non-ionic material such as a polyglycol ether. After a short time, approx. 10 minutes, cool down to approx. 75 C. To the granules thus obtained in the mother liquid, while stirring well, add 0.48 part TNT in a liquid form (temperature of TNT approx. C.). When all the TNT has been added, cool the mixture, and the granules can be drained off on a vacuum filter and dried.

Data for final product:

Sieve analyses: 28.3% remains on sieve No.

U. S. Standard: 71.6% remains between sieve No. 10

and sieve No.

Specific weight: 1.63

It is to be noted that the amount of wax used, as shown by this example or any of the other subsequent examples, can vary in amount of from about 0.5 to 0.005 part. by weight. The wax aids in the producing of bodies from the granules.

The amount of wetting agent used is in the order of about 10 cc. of the wetting agent per ton of the explosive.

, The granulation maybeeiifectuated withoutigse -of a wetting agent.

Example 2 While stirring well, mix at approximately 90 (3., 3.3 Weight parts of water, 1 weight part of cyclonite and 0.2 part of wax, for example, paraffin Wax, a small quantity of wetting agent, as aforesaid and 0.18 part of TNT. The mixing is carried out in a vessel provided with a jacket and a connection at the bottom. Steam is injected directly into the mixture of explosives through the said connection. The steam is used for heating the explosives and the jacket used for cooling. The cooling agent is conducted through the space between the jacket and the vessel. It will be understood of course that steam may also, when desired, be passed therethrough. In the latter case, the explosives will not be heated directly but indirectly. To effectuate an axial flow of the explosives to the vessel, the vessel may be provided with a number of baffles. The stirrer may be provided with obliquely positioned wings. After stirring for about ten minutes, the explosive mixture is cooled to 75 C. To the granules thus produced in the mother liquid and while stirring well, there is added 0.48 weight part of TNT in liquid form, the TNT having a temperature of about 95 C. The TNT is dropped on the mixture from a tube shaped in annular form and provided with holes. When all of the 0.48 part of the TNT has been added, the mixture is cooled to a temperature of 60 C. or even lower. After cooling the granules may be drained oh" and dried.

Data for final product:

Sieve analyses: 28.3% remains on sieve, No. 10

Standard: 71.6% remains between sieve No. 10 and sieve No. 20

Specific weight: 1.63

The procedure just described for carrying out the primary granulation may be varied by first placing the TNT in the mixing vessel, following which the. other explosives can be, put in, While stirring the TNT.

Example 3 Continuous manufacture of granulated mixed explosive containing about 40% TNT (cyclotol 60/40) As shown in the accompanying drawing, there are mixed while, in vessel" 1, per time unit, a water-RDX (cylonite) suspension containing 1 weight portion of RDX, 3.3 parts of water and a suitable wetting agent through supply conduit 1, 0.18 part of TNT and 0.02 part of a suitable liquefied wax are introduced in the vessel through supply pipe 2. The temperature is maintained at approximately 90 C. The primary granules thus formed in vessel I together with the suspending liquid are then transferred through cooling vessel II to vessel III. In vessel III, secondary granulation is carried out by stirring the suspension of the primary granules at a temperature of about 75 C. and spraying the same through the annnlar sprinkler 4 with molten TNT having a temperatureof approximately 95 C. so that, per time unit, 0.48 part of TNT will be added as by coating to the primary granules. The suspension of thethus coated (secondary) granules may then be transferred to vessel IV where the temperature is reduced to about 70 C.; and thence from of t lie inventionand the examples set forth are merely granules first produced.

4 vessel IV to vessel V where the temperature is further reduced to about 50 C. After this last cooling, the mass is discharged and drained off as by means of a vacuum filter and the secondary granules dried.

When using vessels having a cubic capacity of 4 cubic meters, the mixed explosive can be manufactured with a throughput of about 3 tons per hour. I

Data for final product in accordance with this example:

Sieve analyses: 25.0% remains on sieve No. 10 i p U. S. Standard: 74.8% remains between sieve No. 10 and i sieve No. 20 Specific weight: 1.63.

It will be understood that the foregoing description illustrative of the principles thereof. Accordingly, the appended claims are to be construed as defining the in vention within the full spirit and scope thereof. Y

I claim: 1. A method of manufacturing granulatedmixed ex plosive containing trinitrotoluol in excess of 20% whic comprises stirring a suspension of at leastone' explosiv selected from the group consisting of cyclotrimethylenetrinitramine, 2,4,6-trinitro phenylmethylnitramine, pentaerythritol tetranitrate and ammonium picrate and a po tion of the TNT, about one third of the total TNT, i the fluid state in a liquid, cooling the said mixture to temperature whereby homogeneous, uniform, non-stick ing granules. are produced, followed by the step of sus pending the aforesaid granules in Water, stirring the sam and adding thereto the remainder of molten TNT thereby to produce a coating of TNT on the granules first pro-g duced. 2. A method of manufacturing granulated mixed ex plosives containing trinitrotoluol in excess of 20% char-i acterized by the feature that the granules are made two stages, the first stage being one in which the com-it, ponents of the mixed explosives selected'from the grout! consisting of cyclotrimethylenetrinitramine, 2,4,6-01- nitro phenylmethylnitramine, pentaerythritol tetranitrafl and ammonium picrate are suspended in water andstirfed. at a temperature exceeding the melting point of the adding to said stirred suspension a portion of the T about one third of the total TNT and cooling the mixture to a temperature whereby homogeneous, similan, non-sticking primary granules are produced, followed-h! a second stage, wherein said primary granules are pended in water and while being stirred, thereis addd thereto the remainder of molten TNT, thereby to produkt a coating of TNT on the said primary granules. I 3. A method of manufacturing granulated mixed plosives; containing trinitrotoluol in excess of 20% which i. comprises suspending the explosives selected from tll group consisting of cyclotrirnethylenetrinitramine, 2,4,6 w trinitro phenylmethylnitramine, pentaerythritol tetranij trate and ammonium picrate in water, stirringthe samij at a temperature exceeding the melting point of the TNT adding to said stirred suspension a portion of the TNT, about one third of the total TNT and cooling the said mixture to a temperature whereby homogeneous, form, non-sticking granules are produced, followed 1 the step of suspending the aforesaid granulesin water; stirring the same, and adding thereto the remainder of molten TNT thereby to. produce. a coating of TNT on 4. A method of manufacturing a granulated explosive containing trinitrotoluol in excess of 20% RDX which comprises, suspending the RDX'in watcr anfi stirring the same ata temperature exceeding the mel point: of the TNT, adding to such stirred suspension portion of the TNT, about one third of the total I cooling said mixture to a temperature whereby homo geneous, uniform, non-sticking granules of a mixtures! RDX and TNT are produced, suspending said granum 5 in water, stirring the same and adding thereto the re- 2,274,822 mainder of molten TNT, thereby to produce a coating 2,384,730 of TNT on the granules first produced. 2,394,449 2,482,091 References Cited in the file of this patent 5 1 UNITED STATES PATENTS 723 641 1,310,848 Teeple July 22, 1919 6 Cairns et a1. Mar. 3, 1942 Davis et a1. Sept. 11, 1945 Herzog Feb. 5, 1946 Audrieth et a1 Sept. 20, 1949 FOREIGN PATENTS Great Britain Feb. 9, 1955

Patent Citations
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Referenced by
Citing PatentFiling datePublication dateApplicantTitle
US3882208 *Sep 30, 1970May 6, 1975Us NavyMethod for production of spherical particles of a solid material
US4714572 *Sep 26, 1986Dec 22, 1987Nobel Kemi AbTwo-stage granulation of hexotonal and oxtonal; wet processing
US5197677 *Apr 26, 1991Mar 30, 1993Thiokol CorporationExplosives
US5279492 *Feb 25, 1992Jan 18, 1994Thiokol CorporationProcess for reducing sensitivity in explosives
EP0218566A1 *Sep 17, 1986Apr 15, 1987Nobel Kemi ABA method for the manufacture of composite explosives
WO1990005124A1 *Jul 13, 1989May 17, 1990Rheinmetall GmbhProcess for manufacturing explosive charges from non-pourable mixtures
U.S. Classification149/13, 264/3.6, 149/109.6, 149/92, 149/111, 149/107, 427/220, 149/93
International ClassificationC06B21/00, C06B45/26
Cooperative ClassificationC06B21/0066, C06B45/26, Y10S149/111
European ClassificationC06B21/00C8, C06B45/26