US3085047A - Stabilization of diphenylaminechlorarsine gas generating charges by coating the particles with a drying oil - Google Patents
Stabilization of diphenylaminechlorarsine gas generating charges by coating the particles with a drying oil Download PDFInfo
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- US3085047A US3085047A US62217A US6221760A US3085047A US 3085047 A US3085047 A US 3085047A US 62217 A US62217 A US 62217A US 6221760 A US6221760 A US 6221760A US 3085047 A US3085047 A US 3085047A
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- diphenylaminechlorarsine
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- PBNSPNYJYOYWTA-UHFFFAOYSA-N adamsite Chemical compound C1=CC=C2[As](Cl)C3=CC=CC=C3NC2=C1 PBNSPNYJYOYWTA-UHFFFAOYSA-N 0.000 title claims description 47
- 239000002245 particle Substances 0.000 title claims description 46
- 238000001035 drying Methods 0.000 title claims description 16
- 239000011248 coating agent Substances 0.000 title claims description 4
- 238000000576 coating method Methods 0.000 title claims description 4
- 230000006641 stabilisation Effects 0.000 title description 3
- 238000011105 stabilization Methods 0.000 title description 3
- 239000000446 fuel Substances 0.000 claims description 25
- 239000003381 stabilizer Substances 0.000 claims description 17
- 230000001458 anti-acid effect Effects 0.000 claims description 13
- 238000002156 mixing Methods 0.000 claims description 13
- 239000000020 Nitrocellulose Substances 0.000 claims description 11
- 229920001220 nitrocellulos Polymers 0.000 claims description 11
- IMACFCSSMIZSPP-UHFFFAOYSA-N phenacyl chloride Chemical compound ClCC(=O)C1=CC=CC=C1 IMACFCSSMIZSPP-UHFFFAOYSA-N 0.000 claims description 11
- 238000000034 method Methods 0.000 claims description 10
- 239000003921 oil Substances 0.000 claims description 8
- 239000003795 chemical substances by application Substances 0.000 claims description 6
- 239000007789 gas Substances 0.000 description 20
- DMBHHRLKUKUOEG-UHFFFAOYSA-N diphenylamine Chemical compound C=1C=CC=CC=1NC1=CC=CC=C1 DMBHHRLKUKUOEG-UHFFFAOYSA-N 0.000 description 18
- 235000021388 linseed oil Nutrition 0.000 description 14
- 239000000944 linseed oil Substances 0.000 description 14
- 239000000463 material Substances 0.000 description 13
- 239000000203 mixture Substances 0.000 description 11
- VTYYLEPIZMXCLO-UHFFFAOYSA-L Calcium carbonate Chemical compound [Ca+2].[O-]C([O-])=O VTYYLEPIZMXCLO-UHFFFAOYSA-L 0.000 description 8
- VEXZGXHMUGYJMC-UHFFFAOYSA-N Hydrochloric acid Chemical compound Cl VEXZGXHMUGYJMC-UHFFFAOYSA-N 0.000 description 8
- 239000000843 powder Substances 0.000 description 8
- 235000019198 oils Nutrition 0.000 description 7
- 239000003491 tear gas Substances 0.000 description 7
- 238000004519 manufacturing process Methods 0.000 description 6
- 239000002341 toxic gas Substances 0.000 description 6
- 239000012535 impurity Substances 0.000 description 5
- 230000032683 aging Effects 0.000 description 4
- 230000004888 barrier function Effects 0.000 description 4
- 239000004215 Carbon black (E152) Substances 0.000 description 3
- OEYOHULQRFXULB-UHFFFAOYSA-N arsenic trichloride Chemical compound Cl[As](Cl)Cl OEYOHULQRFXULB-UHFFFAOYSA-N 0.000 description 3
- 229930195733 hydrocarbon Natural products 0.000 description 3
- 150000002430 hydrocarbons Chemical class 0.000 description 3
- 239000007788 liquid Substances 0.000 description 3
- 230000000087 stabilizing effect Effects 0.000 description 3
- 239000000126 substance Substances 0.000 description 3
- 231100000331 toxic Toxicity 0.000 description 3
- 230000002588 toxic effect Effects 0.000 description 3
- HJTAZXHBEBIQQX-UHFFFAOYSA-N 1,5-bis(chloromethyl)naphthalene Chemical compound C1=CC=C2C(CCl)=CC=CC2=C1CCl HJTAZXHBEBIQQX-UHFFFAOYSA-N 0.000 description 2
- GOLCXWYRSKYTSP-UHFFFAOYSA-N arsenic trioxide Inorganic materials O1[As]2O[As]1O2 GOLCXWYRSKYTSP-UHFFFAOYSA-N 0.000 description 2
- 229910000019 calcium carbonate Inorganic materials 0.000 description 2
- 235000010216 calcium carbonate Nutrition 0.000 description 2
- 230000000052 comparative effect Effects 0.000 description 2
- 239000000470 constituent Substances 0.000 description 2
- 230000003111 delayed effect Effects 0.000 description 2
- 238000010586 diagram Methods 0.000 description 2
- 238000000227 grinding Methods 0.000 description 2
- -1 if any Substances 0.000 description 2
- 239000004859 Copal Substances 0.000 description 1
- LFQSCWFLJHTTHZ-UHFFFAOYSA-N Ethanol Chemical compound CCO LFQSCWFLJHTTHZ-UHFFFAOYSA-N 0.000 description 1
- 241000782205 Guibourtia conjugata Species 0.000 description 1
- 206010028813 Nausea Diseases 0.000 description 1
- 239000004698 Polyethylene Substances 0.000 description 1
- 239000004793 Polystyrene Substances 0.000 description 1
- 241000779819 Syncarpia glomulifera Species 0.000 description 1
- 239000000654 additive Substances 0.000 description 1
- 230000000996 additive effect Effects 0.000 description 1
- 235000013871 bee wax Nutrition 0.000 description 1
- 239000012166 beeswax Substances 0.000 description 1
- 230000006835 compression Effects 0.000 description 1
- 238000007906 compression Methods 0.000 description 1
- 238000011109 contamination Methods 0.000 description 1
- 238000010924 continuous production Methods 0.000 description 1
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- 230000002427 irreversible effect Effects 0.000 description 1
- 239000002085 irritant Substances 0.000 description 1
- 231100000021 irritant Toxicity 0.000 description 1
- 239000001739 pinus spp. Substances 0.000 description 1
- 229920000573 polyethylene Polymers 0.000 description 1
- 229920002223 polystyrene Polymers 0.000 description 1
- 238000002360 preparation method Methods 0.000 description 1
- 230000000717 retained effect Effects 0.000 description 1
- 230000002441 reversible effect Effects 0.000 description 1
- 239000004576 sand Substances 0.000 description 1
- WKQCYNCZDDJXEK-UHFFFAOYSA-N simalikalactone C Natural products C1C(C23C)OC(=O)CC3C(C)C(=O)C(O)C2C2(C)C1C(C)C=C(OC)C2=O WKQCYNCZDDJXEK-UHFFFAOYSA-N 0.000 description 1
- 239000000779 smoke Substances 0.000 description 1
- 239000007787 solid Substances 0.000 description 1
- 239000002904 solvent Substances 0.000 description 1
- 239000007858 starting material Substances 0.000 description 1
- 238000003860 storage Methods 0.000 description 1
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- 230000002459 sustained effect Effects 0.000 description 1
- 229920003002 synthetic resin Polymers 0.000 description 1
- 239000000057 synthetic resin Substances 0.000 description 1
- 231100000167 toxic agent Toxicity 0.000 description 1
- 239000003440 toxic substance Substances 0.000 description 1
- 229940036248 turpentine Drugs 0.000 description 1
- 239000001993 wax Substances 0.000 description 1
Images
Classifications
-
- C—CHEMISTRY; METALLURGY
- C06—EXPLOSIVES; MATCHES
- C06D—MEANS FOR GENERATING SMOKE OR MIST; GAS-ATTACK COMPOSITIONS; GENERATION OF GAS FOR BLASTING OR PROPULSION (CHEMICAL PART)
- C06D7/00—Compositions for gas-attacks
Definitions
- the device When ignited, the device produces a cloud of toxic smoke with or without an accompanying amount of irritant such as tear gas in the cloud, depending, of course, on the selection of constituent materials desired for the purposes of the charge.
- irritant such as tear gas in the cloud
- These devices include but are not limited to grenades, projectiles, and bank and prison gun cartridges.
- the toxic agent is a sternutatory (sneeze gas) material consisting of vaporized diphenylaminechlorarsine. It liberates as a nausea-causing cloud when commercial diphenylaminechlorarsine is vaporized by means of a nitrocellulose fuel present in the charge, preferably smokeless powder. Due to the stabilizer provided according to the present invention, the age-deterioration process of the charge or, more especially, of the smokeless powder is delayed sufficiently to materially increase the surveillance life.
- a stabilizer is mixed with the commercial diphenylaminechlorarsine prior to the time at which the anti-acid and the tear gas material, if any, and fuel are added and admixed therewith.
- this mixture is charged into the finished gas grenade casing, the result is a delay of the perceptible aging as long as practicably desirable so far as burning time is concerned; replacement of the charges can safely be delayed many months longer than before.
- FIGURE 1 is a block flow diagram of the manufacture of a gas grenade according to the present invention.
- FIGURE 2 shows a modified part of the ow diagram of FIGURE 1;
- FIGURE 3 is a graph of comparative performances showing grenade discharge time plotted against the grenade age.
- a manufacture ow sheet according to a preferred embodiment of the invention takes the appearance of FIGURE 1. It involves the following steps:
- Step I A quantity of dry commercial-grade (crude) diphenylaminechlorarsine particles and a quantity of a stabilizer in liquid or molten form, or as a solution, are placed in a commercial Globe mixer and thoroughly mechanically mixed so as to coat the particles.
- the purpose of the stabilizer is to form a continuous coat or lm impermeable to and mutually insoluble with diphenylamine, diphenylaminechlorarsine and smokeless powder.
- the coat on cooling, may stick the particles together, in which case grinding will be necessary to break their adherence.
- Step II In case the coat is a liquid stabilizer, such as an appropriate drying oil, or else a stabilizer in solution form, the damp particles leaving the mixer '10 are introduced to and kept upon drying trays 12 for a day or for a few days in order to properly dry. The particles are thus stabilized.
- a liquid stabilizer such as an appropriate drying oil, or else a stabilizer in solution form
- Step III The stabilized particles, together with an anti-acid and a quantity of fuel, are introduced into a rotating bottle mixer indicated at 14, the bottles of which are covered to prevent contamination. Mixing within the bottles produces a loose, dry mix.
- the proportions of the mixture are such that it contains by weight 50% to of the nitrocellulose fuel, 5% to 10% of precipitated chalk (CaCO3) as the anti-acid material, and the balance stabilized diphenylaminechlorarsine.
- Step IV The dry mix is introduced and compressed into a grenade case by an operation indicated at 16.
- the compression pressure is quite high, running to a figure approximately between 1 and 2 tons per square inch.
- Step V rl ⁇ he iinal assembly operation for the grenade is indicated by the reference numeral 18.
- the finished gas grenade is indicated at 20 in FIGURE l, incorporating the stabilized charge.
- diphenylaminechlorarsine powder of commercial grade having a particle size which pass a 20- mesh screen are added in the foregoing Step I for each part of the stabilizer liquid consisting of boiled linseed oil.
- the amount of the linseed oil is sufficient to give the mixture the consistency of damp sand, the actual proportions being such that the ratio of diphenylaminechlorarsine to linseed oil therein ranges from 11:1 to 7:1 by weight, with the preferred ratio being 9:1.
- the damp mix in accordance with foregoing Step II, is placed on drying trays and air-dried.
- Boiled linseed oil when completely exposed to the air, is known to dry completely hard in 24 hours; but the preferred time of drying is several days in Step II hereof. It is a characteristic of this particular drying oil that it is absorbed sufficiently that the particles do not stick together; in view of this noncohesive characteristic, no grinding apart of the dried particles is necessary.
- the oxidized oil is a continuous lm around each particle of the diphenylaminechlorarsine so as to be impervious thereto as a barrier isolating the diphenylaminechlorarsine and its impurities from the smokeless powder fuel added according to foregoing Step III.
- the charge is the same ⁇ as hereinabove from standpoint of shelf stability; however, there is a noticeably undesirable sacrifice of economy due to the added amount of linseed oil required for the bulk of the fuel.
- Step IA If parafiin is substituted for linseed oil as the stabilizer, resulting in a step which can be identified as Step IA, then this corresponding step differs to the extent that the parain or other appropriate solid hydrocarbon is preferably melted and applied in the mixer to the diphenylaminechlorarsine so as to coat the powder particles before the hydrocarbon cools.
- the dry mix operation becomes a modified Step IIIA, because of the disadvantage posed that the charge will require a greater proportion of fuel to be added in such Step IIIA.
- the step requires more of the nitrocellulose fuel because the barrier coat of hydrocarbon must also be vaporized during the firing of the charge.
- Step IB If natural waxes, such as copal, beeswax, or the like, or if synthetic resins (e.g., polyethylene or polystyrene) are used as the substitute stabilizer in a further modified step which can be identified as Step IB, then in those instances they can be added either in molten state or added in solution of which turpentine or alcohol, for example, is the solvent. In either case, they dry to form the impervious stabilizer coat on the diphenylaminechlorarsine particles of powder.
- synthetic resins e.g., polyethylene or polystyrene
- a manufacture flow chart illustrative of a preferred embodiment of the invention for combined grenades, takes the appearance in part of FIGURE 2. It includes the foregoing Steps I and II, but the next step is a modified Step IIIC which introduces the tear gas material at the same time at which the fuel and other substances are added preparatory to the dry mixing Step IV. Step IV and Step V are the same as before.
- the anti-acid is indicated as added at 22 and consists of precipitated chalk, as before. Also added is the tear gas material chloracetophenone identified as CN. The precipitated chalk will also stabilize the CN.
- the diphenylaminechlorarsine stabilized in the manner of the preceding description is indicated by the block 26 and fuel is indicated by the double block 28, which is doubled in the drawing merely to indicate more of the same fuel. In other words, some larger amount of such nitrocellulose fuel 28 is required in this instance to be added in the mixing operation, indicated at 30, because of the additional fuel required in this instance to vaporize the tear gas material CN.
- the proportions of the charge resulting from the mixing operation 30 are such that the ratio of materials contained is 50% to 80% of the nitrocellulose fuel, 5% to composed of the block 22 of anti-acid, and the balance consisting of the stabilized diphenylaminechlorarsine and the CN material.
- This balance has proportions such that the ratio of stabilized toxic gas producing material to the tear gas producing material ranges between 4:1 and 1:4 by weight for proper effectiveness of each gas constituent in the blended cloud of gas.
- a grenade so charged is referred to herein as a combined grenade.
- the significance of ythe stabilized low burning time for the improved grenades according to the curve 32 is that, once ignited, the time interval for re-tossing or tampering with these grenades as a practical matter is too short and a presently improved grenade two years old or older can be relied upon ⁇ to rapidly expend itself once ignited with Ilittle chance of meantime being disturbed by human hands.
- the toxic gas producing material diphenylaminechlorarsine in pure state hereinafter referred to as pure DM((C6H4)2NHAsCl), has the following structural formula:
- Diphenylaminechlor-arsine is never pure commercially like the 4above structural formula shows. Only about 70% to is the pure DM and the balance consists of impurities, the presence of which is most readily understood from considering one of the commerical ways of producing diphenylaminechlorarsine.
- the starting material is diphenylamine (C6H5NHC6H5) which is reacted with arsenic trichloride, producing hydrochloric acid along with the wanted diphenylaminechlorarsine as follows:
- hydrochloric acid is present which is not removed from the commercial diphenylaminechlorarsine.
- Equation 2 -above is not irreversible and, in addition to the unreacted diphenylamine, if any, which is present, there is an equilibrium point reached in the reverse direction accounting for the presence of further of the diphenylamine as follows:
- the stabilizing barrier on the particles of the diphenylaminechlorarsine is impermeable to and mutually insoluble with the diphenylamine and is inert insofar as chemically attacking or lbeing chemically attacked by the diphenylamine.
- the reason for isolating the particles of crude diphenylaminechlorasine with a coat is additionally believed necessary because the pure DM content therein tends to break down, analogously to Equation 4 by hydrolizing or for other reasons, over a period of months or years so as to further supplement the quantity of diphenylamine.
- the extreme imperviousness of the coat to' the diphenylamine in particular is felt to account yfor the fuel being retained in a fast burning status without physical impairment upon aging while in the charge.
- the impurities which might impair or attack the fuel can generally be accounted for, one item being the arsensic which, of course, as above indicated, hydrolizes into a fairly inert oxide.
- the presence of the anti-acid chalk insures that the hydrochloric acid, if it escapes from inside .the particles in any quantity, will be automatically neutralized as follows:
- the chalk is commonly referred to in the grenade field as a stabilizer.
- the practice of the present inventions in the manufacture of a toxic gas charge is such that, except for a barely perceptible trend in lthe first few months, the charges stabilize as rto burning time so that to be consistent over the course of months up to three or four years or more.
- This advantage leads to much greater reliability for prison, police, and armed service work, and to considerable gains in economy because of the longer available surveillance life of the present gas grenade.
- An altogether unexpected result of the stabilizer coat has particular significance. That is to say, despite the presumed barrier of an inert coat of oxidized Stabilizer thereabout, the particles are consistently vaporized faster by the fuel in present grenades even when fired fresh.
- the steps comprising coating diphenylaminechlorarsine particles with an impermeable film of stabilizing agent r and thereafter mixing the stabilized diphenylaminechlorarsine particles with a fuel.
- the steps comprising mixing diphenylaminechlorarsine particles with a drying oil, drying the mixture in air to coat the individual diphenylaminechlorarsine particles with an impermeable film of oxidized drying oil, and thereafter mixing the stabilized diphenylaminechlorarsine particles with a fuel.
- the steps comprising mixing diphenylaminechlorarsine particles with linseed oil, drying the mixture in air to coat the individual diphenylaminechlorarsine particles with an impermeable film of oxidized linseed oil, and thereafter mixing the stabilized diphenylaminechlorarsine particles with a fuel and an anti-acid agent.
- the steps comprising mixing diphenylaminechlorarsine particles with linseed oil, drying; the mixture in air Ito coat the individual diphenylaminechlorarsine particles with an impermeable ltilm of oxidized linseed oil, and thereafter mixing the stabilized diphenylaminechlorarsine particles with a fuel, chloracetophenone and an anti-acid agent.
- a gas generating charge consisting essentially, by weight, of -S0% nitrocellulose particles, 510% of an anti-acid agent, and the balance of diphenylaminechlorarsine particles each coated with an impermeable film of oxidized drying oil, the nitrocellulose particles being uncoated.
- a gas generating charge consisting essentially, by weight, of 50-80% nitrocellulose particles, chloracetophenone particles, 5-l0% of an antiacid agent, and the balance of diphenylaminechlorarsine particles each coated with an impermeable film of oxidized drying oil, the nitrocellulose particles being uncoated.
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Description
United States Patent O 3,085,047 STABILIZATION OF DIPHENYLAMINECHLORAR- SINE GAS GENERATING CHARGES BY COAT- ING THE PARTICLES WITH A DRYING OIL Carl R. Weinert, Pittsburgh, Pa., assignor to Federal Laboratories, Inc., Saltsburg, Pa., a corporation of Penn- Sylvania Filed Oct. 13, 1960, Ser. No. 62,217 8 Claims. (Cl. 167-47) The present invention relates to the manufacture of a gas grenade or other device having stabilized diphenylaminechlorarsine included in the gas-generating charge thereof, and to the method of so stabilizing that charge for producing lengthened surveillance life of the grenade. When ignited, the device produces a cloud of toxic smoke with or without an accompanying amount of irritant such as tear gas in the cloud, depending, of course, on the selection of constituent materials desired for the purposes of the charge. These devices include but are not limited to grenades, projectiles, and bank and prison gun cartridges.
lt has been found in practice that toxic gas grenades or combined toxic and tear gas grenades have a limited useful shelf life, not because of their failure with aging to thereafter generate gas when iired, but because, by then, the burning time will have slowed down too much for the grendaes to be effective if, in fact, they can be relied upon at all and at the same time be predictable with some degree of accuracy. Therefore, it is the practice to periodically replace the different stocks of toxic or combination grenades in prisons and in government and police arsenals. The reasons for fast burning and rapid gas evolution are practical-one having to do with the surprise factor of an overwhelming amount of gas being developed all at once, which is a big element in dispersing a mob of rioters. Moreover, an accelerated rate of burning enabling a grenade to expend itself is a great deterrent against having a grenade tossed away by the rioters or, worse, tossed back.
In the gas cloud produced by a grenade according to the present invention, the toxic agent is a sternutatory (sneeze gas) material consisting of vaporized diphenylaminechlorarsine. It liberates as a nausea-causing cloud when commercial diphenylaminechlorarsine is vaporized by means of a nitrocellulose fuel present in the charge, preferably smokeless powder. Due to the stabilizer provided according to the present invention, the age-deterioration process of the charge or, more especially, of the smokeless powder is delayed sufficiently to materially increase the surveillance life.
More particularly, in the preparation of the diphenylaminechlorarsine of the present charge, a stabilizer is mixed with the commercial diphenylaminechlorarsine prior to the time at which the anti-acid and the tear gas material, if any, and fuel are added and admixed therewith. When this mixture is charged into the finished gas grenade casing, the result is a delay of the perceptible aging as long as practicably desirable so far as burning time is concerned; replacement of the charges can safely be delayed many months longer than before.
The foregoing advantages are accomplished by the stabilized charge and means of stabilizing it which comprise my invention, as will now be explained. Features, objects and further advantages are either specifically explained or will become apparent when, for a better understanding of the invention, reference is made to the accompanying drawing which forms a part hereof and in which:
FIGURE 1 is a block flow diagram of the manufacture of a gas grenade according to the present invention;
3,085,047 Patented Apr. 9, 1963 ICC FIGURE 2 shows a modified part of the ow diagram of FIGURE 1; and
FIGURE 3 is a graph of comparative performances showing grenade discharge time plotted against the grenade age.
More particularly, in reference 'to the drawing, a manufacture ow sheet according to a preferred embodiment of the invention takes the appearance of FIGURE 1. It involves the following steps:
Step I: A quantity of dry commercial-grade (crude) diphenylaminechlorarsine particles and a quantity of a stabilizer in liquid or molten form, or as a solution, are placed in a commercial Globe mixer and thoroughly mechanically mixed so as to coat the particles. The purpose of the stabilizer is to form a continuous coat or lm impermeable to and mutually insoluble with diphenylamine, diphenylaminechlorarsine and smokeless powder. In the case of the stabilizer being introduced in molten form, the coat, on cooling, may stick the particles together, in which case grinding will be necessary to break their adherence.
Step II: In case the coat is a liquid stabilizer, such as an appropriate drying oil, or else a stabilizer in solution form, the damp particles leaving the mixer '10 are introduced to and kept upon drying trays 12 for a day or for a few days in order to properly dry. The particles are thus stabilized.
Step III: The stabilized particles, together with an anti-acid and a quantity of fuel, are introduced into a rotating bottle mixer indicated at 14, the bottles of which are covered to prevent contamination. Mixing within the bottles produces a loose, dry mix. The proportions of the mixture are such that it contains by weight 50% to of the nitrocellulose fuel, 5% to 10% of precipitated chalk (CaCO3) as the anti-acid material, and the balance stabilized diphenylaminechlorarsine.
I Step IV: The dry mix is introduced and compressed into a grenade case by an operation indicated at 16. The compression pressure is quite high, running to a figure approximately between 1 and 2 tons per square inch.
Step V: rl`he iinal assembly operation for the grenade is indicated by the reference numeral 18. The finished gas grenade is indicated at 20 in FIGURE l, incorporating the stabilized charge.
Examples which follow of specific ways of accomplishing the stabilization included in the foregoing steps are intended to illustrate the invention for a better understanding. They are by no means exhaustive of the ways possible, being disclosed with the desired purpose of a fuller description and not of limitation.
Examples Several parts of diphenylaminechlorarsine powder of commercial grade having a particle size which pass a 20- mesh screen are added in the foregoing Step I for each part of the stabilizer liquid consisting of boiled linseed oil. The amount of the linseed oil is sufficient to give the mixture the consistency of damp sand, the actual proportions being such that the ratio of diphenylaminechlorarsine to linseed oil therein ranges from 11:1 to 7:1 by weight, with the preferred ratio being 9:1.
The damp mix, in accordance with foregoing Step II, is placed on drying trays and air-dried. Boiled linseed oil, when completely exposed to the air, is known to dry completely hard in 24 hours; but the preferred time of drying is several days in Step II hereof. It is a characteristic of this particular drying oil that it is absorbed sufficiently that the particles do not stick together; in view of this noncohesive characteristic, no grinding apart of the dried particles is necessary. At this point, the oxidized oil is a continuous lm around each particle of the diphenylaminechlorarsine so as to be impervious thereto as a barrier isolating the diphenylaminechlorarsine and its impurities from the smokeless powder fuel added according to foregoing Step III.
If the boiled linseed oil is applied as a coat to the fuel instead of to the diphenylaminechlorarsine, whereafter the coated fuel and the diphenylaminechlorarsine are mixed, the charge is the same `as hereinabove from standpoint of shelf stability; however, there is a noticeably undesirable sacrifice of economy due to the added amount of linseed oil required for the bulk of the fuel.
If parafiin is substituted for linseed oil as the stabilizer, resulting in a step which can be identified as Step IA, then this corresponding step differs to the extent that the parain or other appropriate solid hydrocarbon is preferably melted and applied in the mixer to the diphenylaminechlorarsine so as to coat the powder particles before the hydrocarbon cools. In those instances, the dry mix operation becomes a modified Step IIIA, because of the disadvantage posed that the charge will require a greater proportion of fuel to be added in such Step IIIA. The step requires more of the nitrocellulose fuel because the barrier coat of hydrocarbon must also be vaporized during the firing of the charge.
If natural waxes, such as copal, beeswax, or the like, or if synthetic resins (e.g., polyethylene or polystyrene) are used as the substitute stabilizer in a further modified step which can be identified as Step IB, then in those instances they can be added either in molten state or added in solution of which turpentine or alcohol, for example, is the solvent. In either case, they dry to form the impervious stabilizer coat on the diphenylaminechlorarsine particles of powder.
A manufacture flow chart, illustrative of a preferred embodiment of the invention for combined grenades, takes the appearance in part of FIGURE 2. It includes the foregoing Steps I and II, but the next step is a modified Step IIIC which introduces the tear gas material at the same time at which the fuel and other substances are added preparatory to the dry mixing Step IV. Step IV and Step V are the same as before.
In FIGURE 2, the anti-acid is indicated as added at 22 and consists of precipitated chalk, as before. Also added is the tear gas material chloracetophenone identified as CN. The precipitated chalk will also stabilize the CN. The diphenylaminechlorarsine stabilized in the manner of the preceding description is indicated by the block 26 and fuel is indicated by the double block 28, which is doubled in the drawing merely to indicate more of the same fuel. In other words, some larger amount of such nitrocellulose fuel 28 is required in this instance to be added in the mixing operation, indicated at 30, because of the additional fuel required in this instance to vaporize the tear gas material CN.
Again, the proportions of the charge resulting from the mixing operation 30 are such that the ratio of materials contained is 50% to 80% of the nitrocellulose fuel, 5% to composed of the block 22 of anti-acid, and the balance consisting of the stabilized diphenylaminechlorarsine and the CN material. This balance has proportions such that the ratio of stabilized toxic gas producing material to the tear gas producing material ranges between 4:1 and 1:4 by weight for proper effectiveness of each gas constituent in the blended cloud of gas. A grenade so charged is referred to herein as a combined grenade.
For comparison purposes, two groups of samples of a standard No. 113 toxic gas grenade were made and thereafter tested at intervals, one group being conventional and the other group being made according to the procedure above outlined employing boiled linseed oil as the stabilizer. The burning time performance of the stabilized grenades, when plotted, takes the appearance of the lower curve 32 according to FIGURE 3. It is seen that no substantial aging process is manifest over a course of months or, in fact, two or more years time. On the other hand, the performance of the group of existing type grenade as to burning time takes the appearance of th upper curve 34, from which it can be noted that deterioration with age is sustained as a continuous process with no particular arresting point evident over a course of months or years. During progress of the tests, the trend of each group was so apparent that the tests -were discontinued after approximately two years.
The significance of ythe stabilized low burning time for the improved grenades according to the curve 32 is that, once ignited, the time interval for re-tossing or tampering with these grenades as a practical matter is too short and a presently improved grenade two years old or older can be relied upon `to rapidly expend itself once ignited with Ilittle chance of meantime being disturbed by human hands.
No reason has been exhaustively explored and is known as to why the surveillance life (storage life) has heretofore been limited comparatively drastically. A working hypothesis, however, has been advanced based on chemical considerations of the ingredients of the charge both before and after being introduced into the grenade as finished.
The toxic gas producing material diphenylaminechlorarsine in pure state, hereinafter referred to as pure DM((C6H4)2NHAsCl), has the following structural formula:
Diphenylaminechlor-arsine is never pure commercially like the 4above structural formula shows. Only about 70% to is the pure DM and the balance consists of impurities, the presence of which is most readily understood from considering one of the commerical ways of producing diphenylaminechlorarsine. The starting material is diphenylamine (C6H5NHC6H5) which is reacted with arsenic trichloride, producing hydrochloric acid along with the wanted diphenylaminechlorarsine as follows:
It is thus seen that hydrochloric acid is present which is not removed from the commercial diphenylaminechlorarsine.
The reason for presence of another impurity is due to the fact that Equation 2 -above is not irreversible and, in addition to the unreacted diphenylamine, if any, which is present, there is an equilibrium point reached in the reverse direction accounting for the presence of further of the diphenylamine as follows:
The equilibrium quantity of the arsenic trichloride of chemical Equation 3 and any excess of the arsenic trichloride still present in the commercial production (i.e., that which is unreacted) do not to any material degree remain present in -the commercial grade as such; any substantial -amount will gradually hydrolize as follows:
Each underscored item in the right-hand side of foregoing Equations 2, 3 and 4 is present in each grain of the powder of diphenylaminechlorarsine, of which, as above indicated, the pure DM constitutes only 70% to 901% by weight, with the balance of 30%-10% being composed of the arsenic trioxide (As2O3), diphenylamine, and hydrochloric acid plus the separate particles of chalk (CaCO3) later added as anti-acid, as already described.
Of these impurities and the additive, it is believed that the stabilizing barrier on the particles of the diphenylaminechlorarsine is impermeable to and mutually insoluble with the diphenylamine and is inert insofar as chemically attacking or lbeing chemically attacked by the diphenylamine. The reason for isolating the particles of crude diphenylaminechlorasine with a coat is additionally believed necessary because the pure DM content therein tends to break down, analogously to Equation 4 by hydrolizing or for other reasons, over a period of months or years so as to further supplement the quantity of diphenylamine. The extreme imperviousness of the coat to' the diphenylamine in particular is felt to account yfor the fuel being retained in a fast burning status without physical impairment upon aging while in the charge.
In other respects, the impurities which might impair or attack the fuel can generally be accounted for, one item being the arsensic which, of course, as above indicated, hydrolizes into a fairly inert oxide. The presence of the anti-acid chalk insures that the hydrochloric acid, if it escapes from inside .the particles in any quantity, will be automatically neutralized as follows:
For this reason, the chalk is commonly referred to in the grenade field as a stabilizer.
From the foregoing, it is seen that the practice of the present inventions in the manufacture of a toxic gas charge is such that, except for a barely perceptible trend in lthe first few months, the charges stabilize as rto burning time so that to be consistent over the course of months up to three or four years or more. This advantage leads to much greater reliability for prison, police, and armed service work, and to considerable gains in economy because of the longer available surveillance life of the present gas grenade. An altogether unexpected result of the stabilizer coat has particular significance. That is to say, despite the presumed barrier of an inert coat of oxidized Stabilizer thereabout, the particles are consistently vaporized faster by the fuel in present grenades even when fired fresh. This fact is evidenced by the comparative curves of FIGURE 3 from which the burning time is readily seen to have been speeded up at all points along the curve 32 relative to the reference curve 34 as plotted for grenades with uncoated diphenylaminechlorarsine particles.
Variations within .the `spirit and scope of the inventions described are equally comprehended by the foregoing description.
I claim:
1. In the method of preparing a gas generating charge, the steps comprising coating diphenylaminechlorarsine particles with an impermeable film of stabilizing agent r and thereafter mixing the stabilized diphenylaminechlorarsine particles with a fuel.
2. In the method of preparing a gas generating charge, the steps comprising mixing diphenylaminechlorarsine particles with a drying oil, drying the mixture in air to coat the individual diphenylaminechlorarsine particles with an impermeable film of oxidized drying oil, and thereafter mixing the stabilized diphenylaminechlorarsine particles with a fuel.
3. In the method of preparing .a gas generating charge, the steps comprising mixing diphenylaminechlorarsine particles with linseed oil, drying `the mixture in air to coat the individual diphenylaminechlorarsine particles with an impermeable film of oxidized linseed oil, and thereafter mixing the stabilized diphenylaminechlorarsine particles with a fuel.
4. In .the method of preparing a gas generating charge, the steps comprising mixing diphenylaminechlorarsine particles with linseed oil, drying the mixture in air to coat the individual diphenylaminechlorarsine particles with an impermeable film of oxidized linseed oil, and thereafter mixing the stabilized diphenylaminechlorarsine particles with a fuel and an anti-acid agent.
5. A method according to claim 4, wherein the antiacid agent is precipitated chalk.
6. In the method of preparing a gas generating charge, the steps comprising mixing diphenylaminechlorarsine particles with linseed oil, drying; the mixture in air Ito coat the individual diphenylaminechlorarsine particles with an impermeable ltilm of oxidized linseed oil, and thereafter mixing the stabilized diphenylaminechlorarsine particles with a fuel, chloracetophenone and an anti-acid agent.
7. A gas generating charge consisting essentially, by weight, of -S0% nitrocellulose particles, 510% of an anti-acid agent, and the balance of diphenylaminechlorarsine particles each coated with an impermeable film of oxidized drying oil, the nitrocellulose particles being uncoated.
8. A gas generating charge consisting essentially, by weight, of 50-80% nitrocellulose particles, chloracetophenone particles, 5-l0% of an antiacid agent, and the balance of diphenylaminechlorarsine particles each coated with an impermeable film of oxidized drying oil, the nitrocellulose particles being uncoated.
References Cited in the tile of this patent UNITED STATES PATENTS 1,864,754 Oglesby et al lune 28, 1932 1,878,488 Goss Sept. 20, 1932 2,155,499 Lawson Apr. 25, 1939 2,916,996 Coffee Dec. l5, 1959 FOREIGN PATENTS 25,711 Great Britain Jan. 30, 1897
Claims (2)
1. IN THE METHOD OF PREPARING A GAS GENERATING CHARGE, THE STEPS COMPRISING COATING DIPHENYLAMINECHLORARSINE PARTICLES WITH AN IMPERMEABLE FILM OF STABILIZING AGENT AND THEREAFTER MIXING THE STABILIZED DIPHENYLAMINECHLORARSINE PARTICLES WITH A FUEL
8. A GAS GENERATING CHARGE CONSISTING ESSENTIALLY, BY WEIGHT, OF 50-80% NITROCELLULOSE PARTICLES, CHLORACETOPHENONE PARTICLES, 5-10% OF AN ANTI-ACID AGENT, AND THE BALANCE OF DIPHENYLAMINECHLORARSINE PARTICLES EACH COATED WITH AN IMPERMEABLE FILM OF OXIDIZED DRYING OIL, THE NITROCELLULOSE PATICLES BEING UNCOATED.
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| US62217A US3085047A (en) | 1960-10-13 | 1960-10-13 | Stabilization of diphenylaminechlorarsine gas generating charges by coating the particles with a drying oil |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| US62217A US3085047A (en) | 1960-10-13 | 1960-10-13 | Stabilization of diphenylaminechlorarsine gas generating charges by coating the particles with a drying oil |
Publications (1)
| Publication Number | Publication Date |
|---|---|
| US3085047A true US3085047A (en) | 1963-04-09 |
Family
ID=22040973
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| US62217A Expired - Lifetime US3085047A (en) | 1960-10-13 | 1960-10-13 | Stabilization of diphenylaminechlorarsine gas generating charges by coating the particles with a drying oil |
Country Status (1)
| Country | Link |
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| US (1) | US3085047A (en) |
Cited By (1)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| WO2005102281A3 (en) * | 2004-04-16 | 2010-01-28 | University Of Massachusetts | Porous calcium phosphate networks for synthetic bone material |
Citations (5)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| GB189725711A (en) * | 1897-11-05 | 1898-10-01 | George William Nicholson | Improvements in the Lids or Covers of Saucepans and other like Utensils. |
| US1864754A (en) * | 1924-04-30 | 1932-06-28 | Fed Lab Inc | Process of making a composition for producing irritating gas |
| US1878488A (en) * | 1931-07-13 | 1932-09-20 | Byron C Goss | Generation of persistent disabling gases |
| US2155499A (en) * | 1935-03-23 | 1939-04-25 | Du Pont | Method of waterproofing hygroscopic materials |
| US2916996A (en) * | 1956-02-29 | 1959-12-15 | Olin Mathieson | Propellent powder |
-
1960
- 1960-10-13 US US62217A patent/US3085047A/en not_active Expired - Lifetime
Patent Citations (5)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| GB189725711A (en) * | 1897-11-05 | 1898-10-01 | George William Nicholson | Improvements in the Lids or Covers of Saucepans and other like Utensils. |
| US1864754A (en) * | 1924-04-30 | 1932-06-28 | Fed Lab Inc | Process of making a composition for producing irritating gas |
| US1878488A (en) * | 1931-07-13 | 1932-09-20 | Byron C Goss | Generation of persistent disabling gases |
| US2155499A (en) * | 1935-03-23 | 1939-04-25 | Du Pont | Method of waterproofing hygroscopic materials |
| US2916996A (en) * | 1956-02-29 | 1959-12-15 | Olin Mathieson | Propellent powder |
Cited By (1)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| WO2005102281A3 (en) * | 2004-04-16 | 2010-01-28 | University Of Massachusetts | Porous calcium phosphate networks for synthetic bone material |
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