JPH08303998A - Consolidated propellant and manufacture thereof - Google Patents

Consolidated propellant and manufacture thereof

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Publication number
JPH08303998A
JPH08303998A JP11138295A JP11138295A JPH08303998A JP H08303998 A JPH08303998 A JP H08303998A JP 11138295 A JP11138295 A JP 11138295A JP 11138295 A JP11138295 A JP 11138295A JP H08303998 A JPH08303998 A JP H08303998A
Authority
JP
Japan
Prior art keywords
propellant
solvent
consolidated
particles
ratio
Prior art date
Legal status (The legal status is an assumption and is not a legal conclusion. Google has not performed a legal analysis and makes no representation as to the accuracy of the status listed.)
Withdrawn
Application number
JP11138295A
Other languages
Japanese (ja)
Inventor
Hakobu Umasaki
運 馬崎
Tadaharu Kudo
忠治 工藤
Current Assignee (The listed assignees may be inaccurate. Google has not performed a legal analysis and makes no representation or warranty as to the accuracy of the list.)
Asahi Chemical Industry Co Ltd
Original Assignee
Asahi Chemical Industry Co Ltd
Priority date (The priority date is an assumption and is not a legal conclusion. Google has not performed a legal analysis and makes no representation as to the accuracy of the date listed.)
Filing date
Publication date
Application filed by Asahi Chemical Industry Co Ltd filed Critical Asahi Chemical Industry Co Ltd
Priority to JP11138295A priority Critical patent/JPH08303998A/en
Publication of JPH08303998A publication Critical patent/JPH08303998A/en
Withdrawn legal-status Critical Current

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Abstract

PURPOSE: To provide a consolidated propellant which has a high virtual specific gravity and retains its ability to burn before being consolidated. CONSTITUTION: A grain-shaped propellant consists of a mixture of two kinds of grains, one kind being larger grains and the other kind being smaller grains. The smaller grains have a major axis and a minor axis in ratios of 1.0-2.0. The minor axis of the larger grains is larger than that of the smaller grains by six times or more. As a result, a consolidated propellant obtainable has a high virtual specific gravity and is almost equal in gas-generating velocity to a like product before being consolidated. The consolidation also enables preventing instability of the combustion which may arise in a mixed grain system due to separation between the larger grains and smaller grains in a cartridge case.

Description

【発明の詳細な説明】Detailed Description of the Invention

【0001】[0001]

【産業上の利用分野】本発明は、粒状等の発射薬を溶剤
または接着剤等で固めて成型したコンソリデ−ト発射薬
に関するものである。
BACKGROUND OF THE INVENTION 1. Field of the Invention The present invention relates to a solid propellant formed by solidifying a granular propellant with a solvent or an adhesive.

【0002】[0002]

【従来の技術】銃砲用の弾丸をその初速および射距離を
延ばすためには、砲身を長くするか、または最大許容圧
力を高くする等により達成できる。しかし、システム全
体の重量や大きさの制限からその方法にも限界がある。
そのため、弾丸を発射するための発射薬のエネルギを高
くする試みが行われてきた。
2. Description of the Related Art In order to extend the initial velocity and range of a bullet for a gun, it can be achieved by elongating the barrel or increasing the maximum allowable pressure. However, there is a limit to the method because of the limitation of the weight and size of the entire system.
Therefore, attempts have been made to increase the energy of the propellant for firing bullets.

【0003】発射薬のエネルギを高くするためには、発
射薬成分のエネルギを高くしたり、発射薬のエネルギが
弾丸の運動エネルギへ有効に変換されるように燃焼パタ
ーンを変えたり、あるいは発射薬の量を多くする方法が
考えられてきた。発射薬成分のエネルギを高くする試み
に関しては、新しいエネルギ物質の適用が考えられてい
たが、そのほとんどがまだ実用化されていない。また、
発射薬の燃焼パターンを変える試みに関しては、例えば
米国特許第4581998号明細書に見られるように、
燃焼パターンが燃焼途中で急激に変化するもの等が考案
されている。
In order to increase the energy of the propellant, the energy of the propellant component is increased, the combustion pattern is changed so that the energy of the propellant is effectively converted into the kinetic energy of the bullet, or the propellant is changed. A method of increasing the amount of has been considered. With respect to attempts to increase the energy of propellant components, new energetic materials have been considered, but most of them have not yet been put to practical use. Also,
Attempts to alter the combustion pattern of propellant charge are found, for example, in US Pat. No. 4581998.
A device in which the combustion pattern changes rapidly during combustion has been devised.

【0004】発射薬の量を多くする試みは単に発射薬量
を増加させる方法は薬室の容積が限られているため限界
がある。そのため、例えばコンソリデート発射薬のよう
にグレイ状の発射薬を一定の形を有する成型体に固める
ことにより薬莢内の限られた容積を最大限に使用し、可
能な限り多くの発射薬を装填する方法が考案された。コ
ンソリデート発射薬に関しては、例えばAD−A201
106、AD−A101163、AD−A084680
の技術論文に示されるように、1種類の粒状の発射薬を
溶剤で膨潤させ、それを取り出し成型器に移して圧搾、
成型するか、あるいはニトロセルロース、可塑剤、溶剤
を混ぜたものを発射薬の外表面にコーティングし、それ
を成型器に移して圧搾、成型することにより従来の発射
薬の1.2から1.3倍の仮比重が達成される。なお、
ここで、仮比重とは、単位体積当たりに装填可能な火薬
重量を示す。これらのコンソリデート発射薬を使用する
ことで従来よりもより多くの発射薬を一定容積の薬室に
装填することが可能となる。
Attempts to increase the amount of propellant are simply limited by the limited volume of the chamber. Therefore, by consolidating a gray propellant, such as a consolidate propellant, into a molded body with a certain shape, the maximum amount of the limited volume in the cartridge case is used, and as much propellant as possible is loaded. A method was devised. Regarding the consolidate propellant, for example, AD-A201
106, AD-A101163, AD-A084680
, One type of granular propellant was swelled with solvent, removed and transferred to a molding machine and squeezed,
By molding or coating a mixture of nitrocellulose, a plasticizer and a solvent on the outer surface of the propellant, transferring it to a molding machine and pressing and molding it. A temporary specific gravity of 3 times is achieved. In addition,
Here, the temporary specific gravity indicates the weight of explosive chargeable per unit volume. The use of these consolidate propellants makes it possible to load more propellants into a constant volume chamber than before.

【0005】[0005]

【発明が解決しようとしている課題】しかしながら、こ
の成型方法は圧搾することにより比重を上げるため、当
初の粒状発射薬の性能が損なわれて弾丸の初速が下がっ
てしまい、またその燃焼性能を当初の粒状発射薬の性能
に近づけようとすると比重が下がって目標の性能が達成
できない。
However, since this molding method increases the specific gravity by squeezing, the performance of the initial granular propellant is impaired, the initial velocity of the bullet is lowered, and the combustion performance of the original is lowered. When trying to approach the performance of granular propellant, the specific gravity decreases and the target performance cannot be achieved.

【0006】また、粒状発射薬に孔が貫通している形状
の場合、その孔が圧搾により潰れ発射薬の性能が損なわ
れる問題が発生する。本発明は、仮比重が従来の発射薬
より高く、コンソリデ−ト化前の燃焼性能を保持したコ
ンソリデ−ト発射薬を提供することを課題とするもので
ある。
Further, in the case where the granular propellant has a shape in which a hole penetrates, there is a problem that the hole is crushed by squeezing and the performance of the propellant is impaired. An object of the present invention is to provide a consolidated propellant which has a higher temporary specific gravity than conventional propellants and which retains the combustion performance before consolidation.

【0007】[0007]

【課題を解決するための手段】以上の課題を解決するた
めに、本発明のコンソリデ−ト発射薬は、粒状の発射薬
を用いたコンソリデ−ト発射薬において、粒状発射薬が
大粒子と小粒子との2種類の混合粒子よりなり、前記小
粒子の長軸と短軸との比が1.0〜2.0であり、大粒
子と小粒子との短軸の比が6.0倍以上であることを特
徴とする。
In order to solve the above-mentioned problems, the solid propellant of the present invention is a solid propellant using a granular propellant. It is composed of two kinds of mixed particles with particles, the ratio of the long axis to the short axis of the small particles is 1.0 to 2.0, and the ratio of the short axis of the large particles to the small particles is 6.0 times. The above is characterized.

【0008】本発明のコンソリデ−ト発射薬は、コンソ
リデ−ト化前とコンソリデ−ト化後の仮比重の比が1.
0から1.18の範囲に制御されることが好ましい。
1.18以上大きくするとクローズドボンブ試験結果よ
り以下の式で求められるQ値とコンソリデ−ト化前のQ
値との比率が90パ−セントを切るようになるため好ま
しくない。さらに好ましくは、コンソリデ−ト化前後の
仮比重の比が1.0から1.15が良好である。
The consolidated propellant of the present invention has a ratio of temporary specific gravities before consolidation and after consolidation of 1.
It is preferably controlled in the range of 0 to 1.18.
If it is increased to 1.18 or more, the Q value obtained from the following formula from the closed bomb test result and the Q value before consolidation are calculated.
It is not preferable because the ratio with the value falls below 90 percent. More preferably, the ratio of temporary specific gravities before and after consolidation is 1.0 to 1.15.

【0009】 ここで、Pはクローズドボンブより求められた圧力、t
は時間を示す。また、好ましくは小粒の長軸と短軸の比
が1.0〜2.0であるが、2.0以上になると小粒自
体の仮比重が小さくなり仮比重を上げるという点で問題
になる。また大粒により作られる空間に入りにくくなる
ため、好ましくは1.0〜1.5が良好である。
[0009] Where P is the pressure obtained from the closed bomb, t
Indicates time. Further, the ratio of the major axis to the minor axis of the small particles is preferably 1.0 to 2.0, but if it is 2.0 or more, the temporary specific gravity of the small particles themselves becomes small, which raises a problem in that the temporary specific gravity is increased. Further, it is difficult to enter the space formed by the large particles, so 1.0 to 1.5 is preferable.

【0010】大粒子と小粒子との短軸の比が6.0倍以
上が好ましく、6.0以下になると粒子の分離が発生し
はじめ、製造上の再現性が問題になる。また、仮比重も
大きくならない。大粒子と小粒子との短軸の比が20以
上になると小粒子が小さくなりすぎ、製造上作りにくく
なる。また、大粒子を大きくすると狭い空間に入れる場
合、その大きさが障害になり、装填される発射薬量が大
きくなりにくくなる。そのため、好ましくは大粒子と小
粒子との短軸の比が20以下がよい。但し、これらの単
一寸法の粒子を作るのは製造上難しく、分布を持っても
よい。
The ratio of the short axis of the large particles to that of the small particles is preferably 6.0 times or more, and when the ratio is 6.0 or less, separation of particles begins to occur and reproducibility in manufacturing becomes a problem. Also, the temporary specific gravity does not increase. When the ratio of the short axis of the large particles to the small particles is 20 or more, the small particles become too small, which makes it difficult to make them in manufacturing. Further, when the large particles are made large, when they are put in a narrow space, their size becomes an obstacle, and it becomes difficult to increase the amount of propellant loaded. Therefore, the ratio of the short axis of the large particles to the small particles is preferably 20 or less. However, it is difficult to manufacture these single-sized particles, and they may have a distribution.

【0011】小粒の含有率は重量比で20%〜80%が
好ましく、20%より少なくてもまた80%より多くて
も仮比重は上がらない。本発明に使用する粒状発射薬
は、シングルベ−ス(以下、S/Bという)、ダブルベ
−ス(以下、D/Bという)、トリプルベ−ス(以下、
T/Bという)等を用いることができ、溶剤で膨潤する
高分子を使用した発射薬であれば適用できる。さらに、
粒状発射薬の表面に黒鉛光沢等の表面処理をするのは、
コンソリデ−ト化する前の仮比重を大きくする上で好ま
しい。
The content of the small particles is preferably 20% to 80% by weight, and even if it is less than 20% or more than 80%, the temporary specific gravity does not increase. The granular propellant used in the present invention includes a single base (hereinafter referred to as S / B), a double base (hereinafter referred to as D / B), and a triple base (hereinafter referred to as S / B).
(Referred to as T / B) or the like, and any propellant using a polymer that swells in a solvent can be applied. further,
The surface treatment of graphite propellant such as graphite luster is
It is preferable for increasing the provisional specific gravity before the consolidation.

【0012】さらに、粒状発射薬の形状は、エマルジョ
ン製造法で製造される球状、溶剤圧伸、無用剤圧伸で製
造される円柱、角柱でもよく、円柱、角柱の機軸方向に
貫通する孔が開いていてもよい。例えば、図1に示すよ
うに円柱状発射薬グレイン11の機軸方向に7つの孔1
2が貫通するような発射薬とすることができる。孔は7
孔の他に単孔、19孔等が考えられる。これらの形状は
ガス発生パタ−ンの要求より選定できる。
Further, the shape of the granular propellant may be a spherical shape manufactured by an emulsion manufacturing method, a cylindrical shape manufactured by solvent drawing or a solventless drawing, or a prism, and a hole passing through the cylinder or the prism in the machine axis direction may be used. It may be open. For example, as shown in FIG. 1, there are seven holes 1 in the axial direction of a cylindrical propellant grain 11.
It can be a propellant such that 2 penetrates. 7 holes
In addition to the holes, single holes, 19 holes, etc. can be considered. These shapes can be selected according to the requirements of the gas generation pattern.

【0013】孔が開いている発射薬の場合、孔が無い発
射薬に比較して、圧搾により孔が潰れるためQ値が減少
することがあり、孔を潰さない荷重での圧搾を行い仮比
重を上げる必要がある。コンソリデ−ト化する方法は、
単一溶剤または混合溶剤を用い、発射薬を膨潤させ、金
型等を用い圧搾成型することができる。また、溶剤蒸気
との接触、液体の直接接触で膨潤させることができる
が、直接接触の方が粒状発射薬の表面近傍のみが膨潤し
やすく、中が硬い状態であり、特に孔が開いている場合
は、直接接触で膨潤させるのが好ましい。
In the case of a propellant having a hole, the Q value may be reduced as compared with a propellant having no hole, because the hole is crushed by squeezing. Need to raise. The method of consolidation is
The propellant can be swelled using a single solvent or a mixed solvent, and can be pressed using a mold or the like. Also, it can be swelled by contact with solvent vapor or direct contact with liquid, but direct contact swells only in the vicinity of the surface of the granular propellant, and the inside is hard, especially with holes. In this case, it is preferable to swell by direct contact.

【0014】さらに発射薬の易溶媒のみを用いると発射
薬の膨潤の制御が難しく、易溶媒と難溶剤または非溶剤
との混合溶剤を用いる方がコンソリデ−ト化を制御しや
すい。特に直接接触させる場合は、混合溶剤の使用が好
ましい。易溶媒としては、アセトン、エーテル等のよう
に粒状発射薬を溶解する溶媒が好ましい。難溶剤として
はエチルアルコール等のように粒状発射薬を溶解しない
溶剤が好ましい。非溶剤としてはニトロセルロース等の
ように接着剤として作用するものが好ましい。
Further, it is difficult to control the swelling of the propellant when only the easy solvent of the propellant is used, and it is easier to control the consolidation by using the mixed solvent of the easy solvent and the difficult solvent or the non-solvent. In the case of direct contact, it is preferable to use a mixed solvent. As the easy solvent, a solvent capable of dissolving the granular propellant such as acetone or ether is preferable. As the difficult solvent, a solvent that does not dissolve the granular propellant, such as ethyl alcohol, is preferable. As the non-solvent, those which act as an adhesive such as nitrocellulose are preferable.

【0015】溶剤で膨潤させた後、粒子を移動させ金型
に再装填し圧搾すると装填密度が上がらず、無理に圧搾
することになり、性能を阻害することになる。それ故、
溶剤で膨潤させる容器と圧搾する金型とを同一にし、溶
剤で膨潤させた後、圧搾することが好ましい。例えば、
溶剤で膨潤させる場合、図2に示すように、圧搾用鋳型
22の下方に溶剤抜き用のコック25を設けて粒子が移
動しないようにフィルタ23を配置した鋳型を用意し、
粒子状発射薬24をフィルタ23上に配置し、溶剤を上
から流し込んで粒子状発射薬24を膨潤させて、溶剤抜
き用のコック25から溶剤を抜いて上方から圧搾用治具
21によって圧搾させることができる。
After swelling with a solvent, particles are moved and reloaded in a mold and compressed, the packing density does not increase, and pressing is forcibly performed, which impairs performance. Therefore,
It is preferable that the container to be swollen with a solvent and the mold to be pressed are the same, and the container is swollen with a solvent and then pressed. For example,
In the case of swelling with a solvent, as shown in FIG. 2, a mold 25 in which a filter 25 is arranged so as to prevent particles from moving by providing a cock 25 for removing a solvent below the pressing mold 22 is prepared,
The particulate propellant 24 is placed on the filter 23, the solvent is poured from above to swell the particulate propellant 24, the solvent is removed from the cock 25 for removing the solvent, and is squeezed by the squeezing jig 21 from above. be able to.

【0016】大粒子と小粒子を混合したものを同時に鋳
型に入れ、最密充填すると筋上に分離しやすくなった
り、上下に分離しやすくなる。大粒子を初めに鋳型に入
れ、その後小粒子を入れ、鋳型全体を振動させ大粒子の
空間に小粒子を入れていく方が大粒子と小粒子が分離し
にくい。
If a mixture of large particles and small particles is put into a mold at the same time and the closest packing is carried out, it becomes easy to separate on the streaks, and it becomes easy to separate vertically. It is more difficult to separate the large particles from the large particles when the large particles are first put in the mold, then the small particles are put, and the whole mold is vibrated to put the small particles in the space of the large particles.

【0017】[0017]

【実施例】次に実施例によって本発明をさらに詳細に説
明する。本発明では、S/B、D/BまたはT/Bから
なる大粒子と小粒子を金型に入れ、溶剤を直接接触させ
膨潤させた後に、圧搾成型してコンソリデート発射薬を
形成した。このとき、発射薬を膨潤させる溶剤容器とコ
ンソリデ−ト化する圧搾鋳型を兼用した鋳型の中で発射
薬を膨潤させ、膨潤させた発射薬を移し変えることなく
溶剤との接触を止め、圧搾してコンソリデ−ト化してい
る。
Next, the present invention will be described in more detail by way of examples. In the present invention, large particles and small particles composed of S / B, D / B or T / B were put into a mold, swelled by direct contact with a solvent, and then squeezed to form a consolidate propellant. At this time, swell the propellant in a mold that also serves as a solvent mold for swelling the propellant and a pressing mold for consolidation, and stop contact with the solvent without transferring the swollen propellant and squeeze. Have been consolidated.

【0018】発射薬を膨潤させる溶剤としては、発射薬
の易溶剤と難溶剤の混合溶剤または易溶剤と非溶剤との
混合溶剤を用いた。易溶剤としてはアセトンを用い、難
溶剤としてはエチルアルコールを用い、混合比(重量
比)をアセトン:エチルアルコール=20:80とし
た。また、金型は径50mmのものを用い、圧搾荷重は
2Kgf/cm2 とした。
As a solvent for swelling the propellant, a mixed solvent of an easy solvent of the propellant and a difficult solvent or a mixed solvent of an easy solvent and a non-solvent was used. Acetone was used as the easy solvent, ethyl alcohol was used as the difficult solvent, and the mixing ratio (weight ratio) was acetone: ethyl alcohol = 20: 80. The mold used had a diameter of 50 mm, and the pressing load was 2 Kgf / cm 2 .

【0019】表1から表5に本発明の製造方法によるコ
ンソリデート発射薬を示す。表1および表2は大粒短軸
長/小粒短軸長の影響を示すものである。表1の大粒子
発射薬にはすべてT/Bを用い、小粒子は実施例1、
2、4、5にはD/Bを用い、実施例3、6および比較
例1にはS/Bを用いた。また、表2の大粒子発射薬に
はS/Bを用い、小粒子は実施例9にはD/Bを用い、
実施例7、8、10、11および比較例2にはS/Bを
使用した。小粒比率はすべて0.4とした。
Tables 1 to 5 show the consolidate propellants prepared by the manufacturing method of the present invention. Tables 1 and 2 show the influence of the large grain minor axis length / small grain minor axis length. T / B was used as the large particle propellant in Table 1, and small particles were used in Example 1,
D / B was used for 2, 4 and 5, and S / B was used for Examples 3 and 6 and Comparative Example 1. Further, S / B was used for the large particle propellant in Table 2, D / B was used for the small particle in Example 9, and
S / B was used in Examples 7, 8, 10, and 11 and Comparative Example 2. The small grain ratio was all 0.4.

【0020】[0020]

【表1】 [Table 1]

【0021】[0021]

【表2】 [Table 2]

【0022】表1、表2とも大粒子短軸長/小粒子短軸
長が6.0以上からからDoが増加しはじめ、分離状態
も見られず、クローズドボンブ試験より得られたコンソ
リデート後のQ値とコンソリデート後のQ値の比(Qc
/Qo)も90%以上が達成された。なお、Qc値は直
径約50mm、厚み約25mmのコンソリデ−ト発射薬
を用い、Qo値はコンソリデ−ト発射薬を成型する前の
粒状発射薬を用い、700ccのクロ−ズドボンブ装置
を用いて計測した。
In both Tables 1 and 2, Do started to increase from the large particle minor axis length / small particle minor axis length of 6.0 or more, and no separation state was observed, and after consolidation from the closed bomb test. Ratio of the Q value of Q and the Q value after consolidation (Qc
/ Qo) was also 90% or more. The Qc value was measured using a solid propellant having a diameter of about 50 mm and a thickness of about 25 mm, and the Qo value was measured using a granular propellant before molding the solid propellant, using a 700 cc closed bomb device. did.

【0023】表3、表4は小粒子比率の影響を示すもの
である。表3、表4の大粒子発射薬にはT/Bを用い、
小粒子にはD/Bを用いた。成型法、計測法は、表1お
よび表2と同じ方法を用いた。
Tables 3 and 4 show the influence of the small particle ratio. T / B is used as the large particle propellant in Tables 3 and 4,
D / B was used for the small particles. As the molding method and the measuring method, the same methods as in Table 1 and Table 2 were used.

【0024】[0024]

【表3】 [Table 3]

【0025】[0025]

【表4】 [Table 4]

【0026】表3、表4とも小粒子比率が0.2から
0.8では比重が大きくなっており、Qc/Qoも90
%以上が達成された。表5は小粒子の長軸長/短軸長の
影響を示すものである。表5の大粒子発射薬にはT/B
を、小粒にはD/Bを用いた。成型法、計測法は上記と
同じ方法を用いた。
In Tables 3 and 4, when the small particle ratio is 0.2 to 0.8, the specific gravity is large and the Qc / Qo is 90.
% Or more was achieved. Table 5 shows the influence of the major axis length / minor axis length of the small particles. T / B for large particle propellants in Table 5
, And D / B was used for the small particles. The molding method and the measuring method were the same as above.

【0027】[0027]

【表5】 [Table 5]

【0028】長軸長/短軸長の比が2.0を越えるとコン
ソリデート化前の比重が軽くなり、コンソリデート後の
仮比重をあげるとQc/Qoが90%以下になった。
When the ratio of major axis length / minor axis length exceeds 2.0, the specific gravity before consolidation is reduced, and when the temporary specific gravity after consolidation is increased, Qc / Qo is 90% or less.

【0029】[0029]

【発明の効果】本発明によれば、仮比重が高く、コンソ
リデート化前のガス発生速度とほぼ同等であるコンソリ
デート発射薬が得られるようになる。また、粒状の組合
せの組成制限もなく、ガス発生速度の多様性も持つこと
ができる。さらに混合粒子系で発生する薬莢中での大粒
子と小粒子の分離による燃焼性能の不安定化もコンソリ
デート化により防ぐことが可能となる。
According to the present invention, it is possible to obtain a consolidate propellant having a high temporary specific gravity and having a gas generation rate substantially the same as that before consolidation. Further, there is no limitation on the composition of the granular combination, and the gas generation rate can be varied. Furthermore, it becomes possible to prevent the instability of the combustion performance due to the separation of large particles and small particles in the cartridge case generated in the mixed particle system by consolidating.

【図面の簡単な説明】[Brief description of drawings]

【図1】本発明に使用した円柱状発射薬を示す図であ
る。
FIG. 1 is a view showing a cylindrical propellant used in the present invention.

【図2】本発明に用いられる粒子状発射薬の膨潤と圧搾
鋳型を兼用した鋳型を示す図である。
FIG. 2 is a view showing a mold that also serves as a swelling and swelling mold for the particulate propellant used in the present invention.

【符号の説明】[Explanation of symbols]

11 円柱状発射薬グレイン 12 孔 21 圧搾用治具 22 圧搾用鋳型 23 フィルタ 24 粒子状発射薬 25 溶剤抜き用コック 11 Cylindrical propellant grain 12 Hole 21 Squeeze jig 22 Squeeze mold 23 Filter 24 Particulate propellant 25 Solvent removal cock

Claims (6)

【特許請求の範囲】[Claims] 【請求項1】 粒状の発射薬を用いたコンソリデ−ト発
射薬において、粒状発射薬が大粒子と小粒子との2種類
の混合粒子よりなり、前記小粒子の長軸と短軸との比が
1.0〜2.0であり、大粒子と小粒子との短軸の比が
6.0倍以上であることを特徴とするコンソリデ−ト発
射薬。
1. A consolidated propellant using a granular propellant, wherein the granular propellant is composed of two kinds of mixed particles of large particles and small particles, and the ratio of the major axis to the minor axis of the small particles. Is 1.0 to 2.0, and the ratio of the short axis of the large particles to the small particles is 6.0 times or more, a consolidated propellant.
【請求項2】 小粒の含有比率が重量比率で20%〜8
0%であることを特徴とする請求項1に記載のコンソリ
デ−ト発射薬。
2. The content ratio of small grains is 20% to 8 by weight.
A solid propellant according to claim 1, characterized in that it is 0%.
【請求項3】 コンソリデ−ト化前とコンソリデ−ト化
後の仮比重の比が1.0〜1.18に制御されたことを
特徴とする請求項1または2に記載のコンソリデ−ト発
射薬。
3. The consolidated launch according to claim 1 or 2, wherein the ratio of the temporary specific gravity before consolidation and the temporary specific gravity after consolidation is controlled to 1.0 to 1.18. medicine.
【請求項4】 粒状発射薬は円柱状または角柱状であ
り、機軸方向に貫通孔が配置されていることを特徴とす
る請求項3に記載のコンソリデ−ト発射薬。
4. The solid propellant according to claim 3, wherein the granular propellant has a cylindrical shape or a prismatic shape, and through holes are arranged in the machine axis direction.
【請求項5】 発射薬を膨潤させる溶剤容器とコンソリ
デ−ト化する圧搾鋳型を兼用した鋳型の中で発射薬を膨
潤させ、膨潤させた発射薬を移し変えることなく溶剤と
の接触を止め、圧搾してコンソリデ−ト化することを特
徴とするコンソリデ−ト発射薬の製造方法。
5. A swelling propellant in a mold that also serves as a solvent container for swelling a propellant and a pressing mold for consolidating, stopping contact with the solvent without transferring the swollen propellant, A method for producing a consolidated propellant, comprising squeezing to form a consolidated propellant.
【請求項6】 発射薬を膨潤させる溶剤が発射薬の易溶
剤と難溶剤または非溶剤との混合溶剤であることを特徴
とする請求項5に記載のコンソリデ−ト発射薬の製造方
法。
6. The method for producing a consolidated propellant according to claim 5, wherein the solvent for swelling the propellant is a mixed solvent of an easy solvent for the propellant and a difficult solvent or a non-solvent.
JP11138295A 1995-05-10 1995-05-10 Consolidated propellant and manufacture thereof Withdrawn JPH08303998A (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
JP11138295A JPH08303998A (en) 1995-05-10 1995-05-10 Consolidated propellant and manufacture thereof

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
JP11138295A JPH08303998A (en) 1995-05-10 1995-05-10 Consolidated propellant and manufacture thereof

Publications (1)

Publication Number Publication Date
JPH08303998A true JPH08303998A (en) 1996-11-22

Family

ID=14559770

Family Applications (1)

Application Number Title Priority Date Filing Date
JP11138295A Withdrawn JPH08303998A (en) 1995-05-10 1995-05-10 Consolidated propellant and manufacture thereof

Country Status (1)

Country Link
JP (1) JPH08303998A (en)

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