US2344516A - Propellent powder - Google Patents
Propellent powder Download PDFInfo
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- US2344516A US2344516A US751584A US75158434A US2344516A US 2344516 A US2344516 A US 2344516A US 751584 A US751584 A US 751584A US 75158434 A US75158434 A US 75158434A US 2344516 A US2344516 A US 2344516A
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- nitroglycerine
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- nitrocellulose
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- C—CHEMISTRY; METALLURGY
- C06—EXPLOSIVES; MATCHES
- C06B—EXPLOSIVES OR THERMIC COMPOSITIONS; MANUFACTURE THEREOF; USE OF SINGLE SUBSTANCES AS EXPLOSIVES
- C06B25/00—Compositions containing a nitrated organic compound
- C06B25/18—Compositions containing a nitrated organic compound the compound being nitrocellulose present as 10% or more by weight of the total composition
Definitions
- This invention relates generally to explosives, and particularly to a process of handlingnitro glycerine and treating propellent powders with the same.
- V I a
- propellent powders of the smokeless type which may be, for instance, of a-nitrocellulose base and which are treated with a, deterrent in order to achieve a progressive rateoi combustion and thereby attain improved ballistic characteristics
- the deterrent operates to: retardthe ignitionoi the powder and consequently it. is necessary to employ primers which will produce a hotter flame than would otherwisebe necessary.
- the use of a primer of too' high an energy content-some times imposes an undesirable condition, in that excessive variations in pressure and velocity are occasionally encountered.
- Thehigher energy of the primer although designed to 'oiI-set the deflclencles in the ignitibility of the powder, some-; times promotes conditions in the powder charge which are conducive to more rapid combustion of the powder, and, hence, to the development of excessively high pressures.
- non-hygroscopic such powders mayalsobe surface treatedr with nitroglycerine i which operates as an; accelerator'in thatit renders the powder more readily 1- ignitible and'consequently primers withoutsuch-i exceptionally ihot, flame characteristics may. be: successfully employed with theipropellent charge.
- a more specific object of this invention is to provide .a process powder grains wherein the' procedure is such) as, to avoid the necessity of iteniperaturesfsuch jas wouldtend to oau'se explosions.
- p f Other; objects will become, apparent to those skilled in thei'art: when the following description isread.
- - apropellent powder which' 'may be, tor instance, of v a me, having a .nitrocellulosi t g fli lfbiccleratonlbrj easily ,ignitible 'material,lfsuch,;f instancd asj nitroglycerine wit h',' or f without, a' deterrnt s may be accomplished .byjtreatinglthe nitro' l cellulose in .a'i non-solvent Qbath,f such' as i water," which the nitroglyceritie with; for without; deterrent is amputee;
- The, nitroglycerine con-i tent r the; bath may be regulated" so sgt a trol the; amount which; will j be taken up by the: 'lt being undrstood'that due to the; great amn
- e-t smwad et w h i at x entthetat has els .plate. andustfl n *inlthe form'zof fa; amma; not miscible any lle lw i cib w th1fil tmb $a l m e oaa h sin ire mix u e-. eit tedfl hflvl to cause the lnitroglycerine and nitrocellulose to;
- a man bie v accelerator rent An the c wrlf n lv w th robiqq i-thw yn onl qi m isiea m ke ss.1 r nel nt' ews rt amath u face oi which isigelatinlzed.by 0th 'n accelerato a deterrent.
- the nitrocellulose to be treated may be in the form of substantially completely gelatinized grains as obtained by the extrusion or rolling processes followed by suitable granulating by cutting into discs, flakes, cylinders, etc.; or, the grains may be only partially gelatinized as in the case of, bulk powder grain as used in shot" be of any desired nitrogen content or a blend of nitrocellulose of various nitrogen contents.
- nitroglycerine the nitrates of ethylcne, diethylene', or other glycols may be used, or mixtures of them, with nitroglycerine.
- Other mixtures containing penta-erythrite-tetranitrate, tetranitro-diglycerine may be used in various combinations with, or without, nitroglycerine.
- the nitroglycerine may be I introduced either as asolution or as an emulsion.
- the solvent employed may be one which is, or is not, a solventfor the nitrocellulose. If it is desired to harden the'surface of the grains more than would be accomplished by the nitroglycerine with, or without, deterrent, then a solvent which is also a solvent for the nitrocellulose may be used. Ordinarily, however, it is desired to avoid softening the grains as much as possible and this dictates the use of a solvent for the nitroglycerine which is non-solvent for the nitrocellulose. Ethyl alcohol, benzol, toluene or mixtures thereof, may be used in the latter event while ethyl, butyl, or propyl acetatemay be used where additional hardening is desired.
- Toluene possesses a very distinct advantage in that more concentrated, yet safe, solutions of nitroglycerine may be formed in it than in any other known solvent for nitroglycerine.
- a solution composed of 50 parts nitroglycerine and 50 parts toluene is safe to handle at low temperatures, and in addition such a solution will stand ignition and combustion with less chance of detonation.
- the toluene seems to burn off more slowly and allow concurrent slow combustion of I, the nitroglycerine.
- a deterrent substance such as dinitrotoluene, a dialklylphthalate, or other well known equivalent
- the tendency of the nitroglycerine to detonate, even after the solvent has burnt ofi is very considerably reduced.
- the presence of such a deterrent substance causes combustion to take place more uniformly, and, hence, reduces the tendency of the nitroglycerine to detonate.
- the solvent used in the treatment of nitrocellulose in accordance with this invention may be selected according to the properties desired in the powder and economical and safety considerations. For instance, greater penetration of the nitroglycerine into the grains may be obtained by using toluene than is obtained froman alcohol or benzol. Moreover, when alcohol or alcohol-benzol is used, some of the nitroglycerine may be precipitated due to the solution of alcohol in the water of the bath. This precipitated nitroglycerine will usually be in a very finely dispersed form and will act upon the nitrocellulose surface uniformly and in a manner appreciably different from that encountered in the attack of the nitrocellulose by a benzene or toluene solution of nitroglycerine.
- the solution of nitroglycerine may be introduced directly into the treating bath or may be first emulsified with a small amount of water and then introduced.
- Suitable emulsifying agents such as gum arabic, starch, dextrine and soaps may be used in the latter event.
- nitrocellulose powder grains for example, 300 pounds
- a suitable non-solvent such for instance as water.
- the ratio 0! water to powder grains may be from 3-1 to 10-1 by weight, a practical proportion being 4 parts of water to 1 part of powder grains. This may be agitated to produce a good distribution of the powder grains in the water and then the nitroglycerine may be added in the form of a solution. Water to powder ratios of even less than 3-1 may, in some instances, be used in suitable equipment.
- nitroglycerine may be dissolved in a. vehicle consistingv of seventy-five pounds ethyl alcohol and twenty-five pounds benzol or toluene.
- the nitroglycerine solution thus formed is suitable for treating about 300 pounds of nitrocellulose powder grains, of such a size and character that the resultant powder will give suitable ballistics in a 12. gage shot shell.
- a suitable deterrent such for instance as dibutylphthalate or dinitrotoluene, may also be dissolved in the nitroglycerine solution. It will be understood that the quantity of deterrent employed will depend upon the. circumstances and the type of ammunition into which the resultant powder is to be loaded.
- nitroglycerine solution which may, or may not, contain a deterrent
- the same may be agitated in a. suitable vessel at room temperature for a period of about thirty minutes.
- the temperature of the bath may then be gradually raised to a suitable temperature at which gelatinization of the nitrocellulose powder by nitroglycerine and deterrent, if the latter is employed, may progress.
- a suitable and safe temperature is 65 C. whichmay be reached gradually, as for instance, over a. period of fortyfiveminutes.
- the mixture may be held at this temperature for a period of time sufilcient to accomplish the desired surface gelatinization.
- the nitroglycerine (and deterrent) tends to attack and gelatinize the nitrocellulose leaving the solvent entrained in the bath. However, part of the nitroglycerine probably remains with the solvent, such as benzene or. toluene, and penetrates the nitrocellulose grain in the form of a solution of nitroglycerine. After surface gelatinization and impregnation by the nitroglycerine and deterrent has progressed to the desired extent which may require,'for instance, a period of one hour, the mixture may be cooled down to a suitable temperature for handling as, for instance, 40 C.
- the liquid content may then be discharged from the treated grains in any suitable manner as by draining and/or wringing in a centrifuge.
- the wringing operation may be continued until the moisture content of the treated powder grain has been reduced to less than 30%.
- the spent solvent having given up substantially all its nitroglycerine and deterrent, if thelatter is employed, is discharged with the water and may be disposed of as is desired.
- nitroglycerine containing from -10% of its weight of dinitrotoluene, may be dissolved in toluene to give a solution as concentrated as 30 pounds of nitroglycerine in 30 pounds of toluene.
- This solution may be emulsified with water using a suitable emulsification agent, such as gum arabic, to. give a liquid comprising very finely dispersed droplets of nitroglycerine-dinitrotoluene-toluene solution in water.
- This emulsion is easily distributed in a very uniform manner throughout the water nitrocellulose mixture and is sufficient to treat about 300 pounds of dense powder for sporting ammunition.
- the remaining operations are substantially as described above.
- nitroglycerine solvent which is also solvent for nitrocellulose so as to obtain additional hardening of the grains
- 30 pounds of nitroglycerine may be dissolved in 300 pounds ethyl acetate. This may be distributed in a bath containing about 300 pounds of powder.
- an emulsifying agent such as gum arbaric, starch, dextrine, soap, and the like, is introduced into the treating bath with the nitroglycerine.
- Such materials act as protective colloids and prevent the grains under treatment from sticking together.
- the Y nitroglycerine may be emulsified with water and a sufficiently fine dispersion obtained without any solvent.
- the invention accomplishes its objects and that the process is such as to avoid temperatures such as might tend to cause explosions of the nitroglycerine.
- temperatures and periods of treatment above referred to are merely for the purpose of illustration, they may be varied within limits, it being preferable, however, that substantially none of the solvent employed for the nitroglycerine, with, or without, the deterrent, be evaporated.
- substantially all of the solvent employed for'the' nitroglycerine, after giving up its nitroglycerine and deterrent (if the latter is employed) is discharged as a liquid with the water of the treating bath.
- the powder grains resulting from the proce'ss of the present invention when a deterrent is employed, will have their surfaces gelatinized by both nitroglycerine and the deterrent in view of the fact that the same have been deposited concurrently. In this manner the iballistic characteristics may be more readilycontrolled while favorable ignition properties are maintained and a progressive burning or combustion .rate achieved.
- a non-solvent bath having a solution of nitroglycerine distributed therein.
- the process comprising, treating nitrocellulose powder grains while distributed in a bath of water with nitroglycerine dissolved in a vehicle until the grains are surface gelatinized, elevating the temperature of the mix to an extent sufficient to promote gelatinization of the nitrocellulose by the nitroglycerine but not high enough to vaporize either solvent, the nitroglycerine or the water and removing the vehicle as a liquid.
- the process comprising, concurrently surface the process comprising, concurrently surface 5 treating smokeless powder grains while suspendtreating smokeless powder grains while suspended in anon-solvent bath with nitroglycerine and ed in a non-solvent bath with an accelerator and dinitrotoluene in a solvent capable of penetrating a deterrent in a solvent capable of penetrating the grain. the grain. 14.
- l0 der which comprises, preparingawater bath conthe process comprising, concurrently surface taining smokeless powder grains and a liquid treating smokeless powder grains while suspendnitric ester of a polyhydric alcohol dissolved in ed in a non-solvent bath with nitroglycerine and a solvent therefor, and agitating the bath and a detergent in a solvent capable of penetrating contents sufliciently to distribute the powder the grain. 15 grains and ester solution therein, such agitation 12.
- the process comprising, concurrently surface treating smokeless powder grains while suspended in a non-solvent bath with nitroglycerine and being maintained until the ester is substantially all absorbed by the powder grains.
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Description
Patented Mar. 21, 1944 umr 'PROPELLENT POWDER.
i George A. McBride, Alton, ern Cartridge Company,
7 -porationof Delaware 7 No Drawing.
14 Claims;
This invention relates generally to explosives, and particularly to a process of handlingnitro glycerine and treating propellent powders with the same. V I a In propellent powders of the smokeless type, which may be, for instance, of a-nitrocellulose base and which are treated with a, deterrent in order to achieve a progressive rateoi combustion and thereby attain improved ballistic characteristics, it sometimes happens that the. presence of the deterrent operates to: retardthe ignitionoi the powder and consequently it. is necessary to employ primers which will produce a hotter flame than would otherwisebe necessary. l The use of a primer of too' high an energy content-some times imposes an undesirable condition, in that excessive variations in pressure and velocity are occasionally encountered. Thehigher energy of the primer, although designed to 'oiI-set the deflclencles in the ignitibility of the powder, some-; times promotes conditions in the powder charge which are conducive to more rapid combustion of the powder, and, hence, to the development of excessively high pressures. Experience hasindi--- cated that it is preferableto avoid excessive use of. difficultlydgnitible; coatings onthe powder. In order to render such powdersmore readily ignitible and at the same time more; non-hygroscopic such powders mayalsobe surface treatedr with nitroglycerine i which operates as an; accelerator'in thatit renders the powder more readily 1- ignitible and'consequently primers withoutsuch-i exceptionally ihot, flame characteristics may. be: successfully employed with theipropellent charge.
111115 among, the objects of the present invention to provide; a process gof handling ;nltr,olycerine and treating powder-1 with the -.,'same wherein ,the hazards- ,heretofore encountered in;
such processes willbe substantiallyteliminated Th tor-the re ent 1nvention. enera lystated, isto; provide a safeprocess of treating L kele s, qw r w h e qae ntasu ras n me base, .ni ay be ftre'a'tedflwi nitrocellulose,
111., assignor towe'st East Alton, 111., acor- Application November j 5, 1934.: Serial NO- 751,584 l .v v
A more specific object of this invention is to provide .a process powder grains wherein the' procedure is such) as, to avoid the necessity of iteniperaturesfsuch jas wouldtend to oau'se explosions. p f Other; objects will become, apparent to those skilled in thei'art: when the following description isread. a Y Generally stated, in accordance.with theipres-l ent invention,- apropellent powder which' 'may be, tor instance, of v a me, having a .nitrocellulosi t g fli lfbiccleratonlbrj easily ,ignitible 'material,lfsuch,;f instancd asj nitroglycerine wit h',' or f without, a' deterrnt s may be accomplished .byjtreatinglthe nitro' l cellulose in .a'i non-solvent Qbath,f such' as i water," which the nitroglyceritie with; for without; deterrent is amputee; The, nitroglycerine con-i tent r the; bath may be regulated" so sgt a trol the; amount which; will j be taken up by the: 'lt being undrstood'that due to the; great amnity of nitroglyeerinei for nitrocellulose, substantially all nitroglycerine in the bathwillbetaken pp by the 1 nitrocelluloseflln order to achieve uniformity o'ttreatmehtoi the nitrocellm,
. losejthe'vnitroglycerlnemaylbe vadded to the bath;
e-t smwad et w h i at x entthetat has els .plate. andustfl n *inlthe form'zof fa; amma; not miscible any lle lw i cib w th1fil tmb $a l m e oaa h sin ire mix u e-. eit tedfl hflvl to cause the lnitroglycerine and nitrocellulose to;
i rt a; fie eus 59 ec m m m lulq g en s pnit y fi li;
ate qs c .91 he fia's latm t l e; o inert al; hus sepwted i f fi ss sa f e ee t zationi a lnroe e s ito a in ..1 .9 i, h? t tme t .7 Namin some ,Oib sz o ve v o the. t 'o l tins. may d sc ar ed; rom th 1t (La i av o ti nc, i r' rai -s mete wrin n timazce tntu e i lt s manne celerator is accomplished without subiecting ,the
s i .wh eh i lendr' he pow e mor di ignitibleo and/0 1 moremon-hygroscopic.
A man bie v accelerator rent. An the c wrlf n lv w th robiqq i-thw yn onl qi m isiea m ke ss.1 r nel nt' ews rt amath u face oi which isigelatinlzed.by 0th 'n accelerato a deterrent.
Agstlii iurtherrobl'ec sle -prov il-P of v i n H erinema p main i tr y, hesafel nd ,i ien qisi fdI-to;
ernalzpham eristi he-grains mamvbe1added:
rains, and
atin bathztox tem era ure-stat..- u h or e as Qm ww 1F59- QKPl QQ QEth nitro ly z erin desi d any-suitab solvent;whichacarries hei nitroglycerinei' intorthez; w h, e addition mat ri ls-may senvecsevsc a rrlo tm e y the,;resistance;to; penetration tmoisturie; zTheyi the flowing;- ;characteristics;;;o the;
@0 3 exam e improve:
etc we umformloading .cond
of. surface treating propellen't I t'ions. They may avoid development of static electricity. They may aid the nitroglycerine to penetrate the grain.
The nitrocellulose to be treated may be in the form of substantially completely gelatinized grains as obtained by the extrusion or rolling processes followed by suitable granulating by cutting into discs, flakes, cylinders, etc.; or, the grains may be only partially gelatinized as in the case of, bulk powder grain as used in shot" be of any desired nitrogen content or a blend of nitrocellulose of various nitrogen contents. Instead'of nitroglycerine, the nitrates of ethylcne, diethylene', or other glycols may be used, or mixtures of them, with nitroglycerine. Other mixtures containing penta-erythrite-tetranitrate, tetranitro-diglycerine may be used in various combinations with, or without, nitroglycerine.
As remarked above, the nitroglycerine may be I introduced either as asolution or as an emulsion. The solvent employed may be one which is, or is not, a solventfor the nitrocellulose. If it is desired to harden the'surface of the grains more than would be accomplished by the nitroglycerine with, or without, deterrent, then a solvent which is also a solvent for the nitrocellulose may be used. Ordinarily, however, it is desired to avoid softening the grains as much as possible and this dictates the use of a solvent for the nitroglycerine which is non-solvent for the nitrocellulose. Ethyl alcohol, benzol, toluene or mixtures thereof, may be used in the latter event while ethyl, butyl, or propyl acetatemay be used where additional hardening is desired.
Toluene possesses a very distinct advantage in that more concentrated, yet safe, solutions of nitroglycerine may be formed in it than in any other known solvent for nitroglycerine. A solution composed of 50 parts nitroglycerine and 50 parts toluene is safe to handle at low temperatures, and in addition such a solution will stand ignition and combustion with less chance of detonation. The toluene seems to burn off more slowly and allow concurrent slow combustion of I, the nitroglycerine. By adding to the solution 5-10% by weight oi. a deterrent substance, such as dinitrotoluene, a dialklylphthalate, or other well known equivalent, the tendency of the nitroglycerine to detonate, even after the solvent has burnt ofi is very considerably reduced. The presence of such a deterrent substance causes combustion to take place more uniformly, and, hence, reduces the tendency of the nitroglycerine to detonate.
The solvent used in the treatment of nitrocellulose in accordance with this invention may be selected according to the properties desired in the powder and economical and safety considerations. For instance, greater penetration of the nitroglycerine into the grains may be obtained by using toluene than is obtained froman alcohol or benzol. Moreover, when alcohol or alcohol-benzol is used, some of the nitroglycerine may be precipitated due to the solution of alcohol in the water of the bath. This precipitated nitroglycerine will usually be in a very finely dispersed form and will act upon the nitrocellulose surface uniformly and in a manner appreciably different from that encountered in the attack of the nitrocellulose by a benzene or toluene solution of nitroglycerine. It, therefore, depends to a large degree upon the type of propellent powder grains desired, as to what specific surface characteristics are deliberately produced, and as to whatsolvents are employed. If alcohol is used, it will almost inevitably be lost, due to dilution by the water used in separating the powder grains. The solvents such as toluene and benzene, which are largely nonmiscible with water, can be separated to some extent and recovered, but it may frequently be of an advantage to-use such proportions of solvent with respect to powder, nitroglycerine, and water that substantially all of the toluene, for example, will penetrate the grains and will be removable from the grains during subsequent drying treatments.
The solution of nitroglycerine may be introduced directly into the treating bath or may be first emulsified with a small amount of water and then introduced. Suitable emulsifying agents such as gum arabic, starch, dextrine and soaps may be used in the latter event.
As a practical embodiment which is illustrative of the present invention a charge of nitrocellulose powder grains, for example, 300 pounds, may be incorporated in a suitable non-solvent, such for instance as water. The ratio 0! water to powder grains may be from 3-1 to 10-1 by weight, a practical proportion being 4 parts of water to 1 part of powder grains. This may be agitated to produce a good distribution of the powder grains in the water and then the nitroglycerine may be added in the form of a solution. Water to powder ratios of even less than 3-1 may, in some instances, be used in suitable equipment.
As a specific example of a suitable solution, thirty pounds of nitroglycerine may be dissolved in a. vehicle consistingv of seventy-five pounds ethyl alcohol and twenty-five pounds benzol or toluene. The nitroglycerine solution thus formed is suitable for treating about 300 pounds of nitrocellulose powder grains, of such a size and character that the resultant powder will give suitable ballistics in a 12. gage shot shell.
If desired, a suitable deterrent, such for instance as dibutylphthalate or dinitrotoluene, may also be dissolved in the nitroglycerine solution. It will be understood that the quantity of deterrent employed will depend upon the. circumstances and the type of ammunition into which the resultant powder is to be loaded.
After the nitroglycerine solution, which may, or may not, contain a deterrent, has been added to thewater-nitrocellulose mixture the same may be agitated in a. suitable vessel at room temperature for a period of about thirty minutes. The temperature of the bath may then be gradually raised to a suitable temperature at which gelatinization of the nitrocellulose powder by nitroglycerine and deterrent, if the latter is employed, may progress. A suitable and safe temperature is 65 C. whichmay be reached gradually, as for instance, over a. period of fortyfiveminutes. The mixture may be held at this temperature for a period of time sufilcient to accomplish the desired surface gelatinization. The nitroglycerine (and deterrent) tends to attack and gelatinize the nitrocellulose leaving the solvent entrained in the bath. However, part of the nitroglycerine probably remains with the solvent, such as benzene or. toluene, and penetrates the nitrocellulose grain in the form of a solution of nitroglycerine. After surface gelatinization and impregnation by the nitroglycerine and deterrent has progressed to the desired extent which may require,'for instance, a period of one hour, the mixture may be cooled down to a suitable temperature for handling as, for instance, 40 C.
The liquid content may then be discharged from the treated grains in any suitable manner as by draining and/or wringing in a centrifuge. The wringing operation may be continued until the moisture content of the treated powder grain has been reduced to less than 30%. In this manner the spent solvent having given up substantially all its nitroglycerine and deterrent, if thelatter is employed, is discharged with the water and may be disposed of as is desired.
As another illustrative embodiment, nitroglycerine, containing from -10% of its weight of dinitrotoluene, may be dissolved in toluene to give a solution as concentrated as 30 pounds of nitroglycerine in 30 pounds of toluene. This solution may be emulsified with water using a suitable emulsification agent, such as gum arabic, to. give a liquid comprising very finely dispersed droplets of nitroglycerine-dinitrotoluene-toluene solution in water. This emulsion is easily distributed in a very uniform manner throughout the water nitrocellulose mixture and is sufficient to treat about 300 pounds of dense powder for sporting ammunition. The remaining operations are substantially as described above.
As illustrating the use of a nitroglycerine solvent which is also solvent for nitrocellulose so as to obtain additional hardening of the grains, 30 pounds of nitroglycerine may be dissolved in 300 pounds ethyl acetate. This may be distributed in a bath containing about 300 pounds of powder. Advantageous results are obtained with this, as well as the other embodiments, if about one-fourth percent of an emulsifying agent, such as gum arbaric, starch, dextrine, soap, and the like, is introduced into the treating bath with the nitroglycerine. Such materials act as protective colloids and prevent the grains under treatment from sticking together.
Moreover, by the aid of emulsifying agents the Y nitroglycerine may be emulsified with water and a sufficiently fine dispersion obtained without any solvent.
From the foregoing description it is apparent that the invention accomplishes its objects and that the process is such as to avoid temperatures such as might tend to cause explosions of the nitroglycerine. Although it is to be understood that the temperatures and periods of treatment above referred to are merely for the purpose of illustration, they may be varied within limits, it being preferable, however, that substantially none of the solvent employed for the nitroglycerine, with, or without, the deterrent, be evaporated. By thus maintaining the temperatures of treatment below the vaporizing temperature for the nitroglycerine solvent, it is apparent that the hazardous possibility of nitroglycerine distilling over with the solvent is avoided and the danger of operation thus greatly reduced. In accordance with the present invention substantially all of the solvent employed for'the' nitroglycerine, after giving up its nitroglycerine and deterrent (if the latter is employed) is discharged as a liquid with the water of the treating bath. Moreover, the powder grains resulting from the proce'ss of the present invention, when a deterrent is employed, will have their surfaces gelatinized by both nitroglycerine and the deterrent in view of the fact that the same have been deposited concurrently. In this manner the iballistic characteristics may be more readilycontrolled while favorable ignition properties are maintained and a progressive burning or combustion .rate achieved.
It is apparent that the various features of this invention are not limited in their application to the specific embodiments hereinbefore described, but it is to be understood that the terms nitrocellulose, nitroglycerine deterrent solvent, etc., have been used in an illustrative and not in a limiting sense. It is to be understood, therefore, that the invention is not limited to the specific details herein set forth for the purpose of illustration, but that such modifications and the use of such individual features and sub-combinations of features as may occur to those skilled in the art without departing from the spirit of this invention are, although not specifically described herein, contemplated by and within the scope of the appended claims.
-Having thus described the invention, what is claimed is:
1. In the art of making propellent powders, the process comprising, treating nitrocellulose powder grains while suspended in water with a solution of nitroglycerine and a deterrent.
2. In the art of making propellent powders,
the process comprising, treating nitrocellulose in.
a non-solvent bath having a solution of nitroglycerine distributed therein.
3. In the art of making propellent powders, the process comprising, forming an aqueous suspension of nitrocellulose, and distributing a solution of nitroglycerine throughout the slurry.
4. In the art of making propel ent powders,
the process comprising, treating nitrocellulose powder grains while distributed in a bath of water with nitroglycerine dissolved in a vehicle until the grains are surface gelatinized, elevating the temperature of the mix to an extent sufficient to promote gelatinization of the nitrocellulose by the nitroglycerine but not high enough to vaporize either solvent, the nitroglycerine or the water and removing the vehicle as a liquid.
5. In the art ofmaking propellent powders, the process comprising, treating nitrocellulose powder grains while suspended in water with nitroglycerine and a deterrent dissolved in a vehicle which is non-solvent for the nitrocellulose. Y
6. In the art of making propellent powders, the process comprising,.treating smokeless powder grains with nitroglycerine dissolved in toluene.
.7. In the art of making propellent powders, the process comprising, treating smokeless powder grains with nitroglycerine and dinitrotoluene dissolved in toluene.
8. In the art of making propellent powders, the process comprising, surface treating smokeless powder grains witha nitroglycerine solution in a non-solvent bath, and discharging the bath with theentrained spent nitroglycerine solution from the grains after surface treatment has progressed to the desired extent. I
9. In the art of making propellent powders, the process comprising, suspending smokeless powder grains in a non-solvent vehicle, adding a solution of modifier having an afiinity for the grains, agitating the mixture until the modified trained in the vehicle, and discharging the vehicle with the entrained modifiersolvent.
10. In the art of making propellent powders,
dibutylphthalate in a solvent capable of penetrating the grain.
13. In the art of making propellent powders, the process comprising, concurrently surface the process comprising, concurrently surface 5 treating smokeless powder grains while suspendtreating smokeless powder grains while suspended in anon-solvent bath with nitroglycerine and ed in a non-solvent bath with an accelerator and dinitrotoluene in a solvent capable of penetrating a deterrent in a solvent capable of penetrating the grain. the grain. 14. The process of producing a propellent pow- 11. In the art of making propellent powders, l0 der which comprises, preparingawater bath conthe process comprising, concurrently surface taining smokeless powder grains and a liquid treating smokeless powder grains while suspendnitric ester of a polyhydric alcohol dissolved in ed in a non-solvent bath with nitroglycerine and a solvent therefor, and agitating the bath and a detergent in a solvent capable of penetrating contents sufliciently to distribute the powder the grain. 15 grains and ester solution therein, such agitation 12. In the art of making propellent powders, the process comprising, concurrently surface treating smokeless powder grains while suspended in a non-solvent bath with nitroglycerine and being maintained until the ester is substantially all absorbed by the powder grains.
GEORGE A. MCBRIDE.
CERTIFICATE or CORRECTION. Patent ,No. 2, 51 h, 516. March 21, 191 h.
GEORGE A. MCBRIDE.
It is hereby certified that error appears in the printed specification of the above numbered patent requiring correction as follows: Page 5, second column, line 75, claim 9, for "modified" read -mod1i.ier-; page 1.1., first column, line 114., claim 1l, for "detergent" read --deterrent--; and that the said Letters Patent should be read with this correction therein that the same may conform to the record of the case in the Patent Office.
Signedand sealed this 16th day of May, A. D. 19bi Leslie Frazer Acting Commissioner of Patents.
(Seal) CERTIFICATE OF CORRECTION. Patent No. 2,51%516. March 21, 1 th.
GEORGE A. MCBRIDE.
It is hereby certified that error appears in the printed specification of the above numbered patent requiring correction as follows: Page 5, second column, line 75, claim 9, for "modified" read -modifier--; page 14., first column, line 111., claim 11, for "detergent" read --deterrent-; and that the said Letters Patent should be read with this correction therein that the same may conform to the record of the case in the Patent Office.
Signed and sealed this 16th day of May, A. D. 191 1 Leslie Frazer (Seal) Acting Commissioner of Patents.
Priority Applications (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
US751584A US2344516A (en) | 1934-11-05 | 1934-11-05 | Propellent powder |
Applications Claiming Priority (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
US751584A US2344516A (en) | 1934-11-05 | 1934-11-05 | Propellent powder |
Publications (1)
Publication Number | Publication Date |
---|---|
US2344516A true US2344516A (en) | 1944-03-21 |
Family
ID=25022659
Family Applications (1)
Application Number | Title | Priority Date | Filing Date |
---|---|---|---|
US751584A Expired - Lifetime US2344516A (en) | 1934-11-05 | 1934-11-05 | Propellent powder |
Country Status (1)
Country | Link |
---|---|
US (1) | US2344516A (en) |
Cited By (4)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
US2499295A (en) * | 1945-07-19 | 1950-02-28 | David S Bruce | Art of making propellant powder |
US2787533A (en) * | 1952-12-17 | 1957-04-02 | Olin Mathieson | Propellent powder and method for producing same |
US3676533A (en) * | 1968-06-26 | 1972-07-11 | Hercules Inc | Method of preparing propellant charges from fibrous nitrocellulose |
RU2627407C1 (en) * | 2016-06-22 | 2017-08-08 | Федеральное казенное предприятие "Государственный научно-исследовательский институт химических продуктов" (ФКП "ГосНИИХП") | Spherical powder |
-
1934
- 1934-11-05 US US751584A patent/US2344516A/en not_active Expired - Lifetime
Cited By (4)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
US2499295A (en) * | 1945-07-19 | 1950-02-28 | David S Bruce | Art of making propellant powder |
US2787533A (en) * | 1952-12-17 | 1957-04-02 | Olin Mathieson | Propellent powder and method for producing same |
US3676533A (en) * | 1968-06-26 | 1972-07-11 | Hercules Inc | Method of preparing propellant charges from fibrous nitrocellulose |
RU2627407C1 (en) * | 2016-06-22 | 2017-08-08 | Федеральное казенное предприятие "Государственный научно-исследовательский институт химических продуктов" (ФКП "ГосНИИХП") | Spherical powder |
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