GB2257968A - Preparation of composite double base propellants - Google Patents

Preparation of composite double base propellants Download PDF

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Publication number
GB2257968A
GB2257968A GB8413649A GB8413649A GB2257968A GB 2257968 A GB2257968 A GB 2257968A GB 8413649 A GB8413649 A GB 8413649A GB 8413649 A GB8413649 A GB 8413649A GB 2257968 A GB2257968 A GB 2257968A
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Prior art keywords
process according
base powder
base
propellant
crosslinking agent
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GB2257968B (en
GB8413649D0 (en
Inventor
Rene Couturier
Yves Longevialle
Mauricette Rat
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Societe Nationale des Poudres et Explosifs
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Societe Nationale des Poudres et Explosifs
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    • CCHEMISTRY; METALLURGY
    • C06EXPLOSIVES; MATCHES
    • C06BEXPLOSIVES OR THERMIC COMPOSITIONS; MANUFACTURE THEREOF; USE OF SINGLE SUBSTANCES AS EXPLOSIVES
    • C06B45/00Compositions or products which are defined by structure or arrangement of component of product
    • C06B45/04Compositions or products which are defined by structure or arrangement of component of product comprising solid particles dispersed in solid solution or matrix not used for explosives where the matrix consists essentially of nitrated carbohydrates or a low molecular organic explosive
    • C06B45/06Compositions or products which are defined by structure or arrangement of component of product comprising solid particles dispersed in solid solution or matrix not used for explosives where the matrix consists essentially of nitrated carbohydrates or a low molecular organic explosive the solid solution or matrix containing an organic component
    • C06B45/10Compositions or products which are defined by structure or arrangement of component of product comprising solid particles dispersed in solid solution or matrix not used for explosives where the matrix consists essentially of nitrated carbohydrates or a low molecular organic explosive the solid solution or matrix containing an organic component the organic component containing a resin
    • C06B45/105The resin being a polymer bearing energetic groups or containing a soluble organic explosive
    • CCHEMISTRY; METALLURGY
    • C06EXPLOSIVES; MATCHES
    • C06BEXPLOSIVES OR THERMIC COMPOSITIONS; MANUFACTURE THEREOF; USE OF SINGLE SUBSTANCES AS EXPLOSIVES
    • C06B25/00Compositions containing a nitrated organic compound
    • C06B25/18Compositions containing a nitrated organic compound the compound being nitrocellulose present as 10% or more by weight of the total composition
    • C06B25/24Compositions containing a nitrated organic compound the compound being nitrocellulose present as 10% or more by weight of the total composition with nitroglycerine
    • CCHEMISTRY; METALLURGY
    • C06EXPLOSIVES; MATCHES
    • C06BEXPLOSIVES OR THERMIC COMPOSITIONS; MANUFACTURE THEREOF; USE OF SINGLE SUBSTANCES AS EXPLOSIVES
    • C06B25/00Compositions containing a nitrated organic compound
    • C06B25/34Compositions containing a nitrated organic compound the compound being a nitrated acyclic, alicyclic or heterocyclic amine

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  • Chemical & Material Sciences (AREA)
  • Organic Chemistry (AREA)
  • Health & Medical Sciences (AREA)
  • Life Sciences & Earth Sciences (AREA)
  • Dispersion Chemistry (AREA)
  • Molecular Biology (AREA)
  • Crystallography & Structural Chemistry (AREA)
  • Emergency Medicine (AREA)
  • Polyurethanes Or Polyureas (AREA)
  • Moulding By Coating Moulds (AREA)

Abstract

A composite double base propellant is provided by the in situ casting method, at least one polyisocyanate crosslinking agent being introduced together with the casting solvent into the base powder. The propellant may include nitroglycerin, TMETN, TRENO, BTTN, propanediol dinitrate; a plasticiser such as triacetin, and a stabiliser, such as NDPA, centralite or N-methyl-para-nitroaniline.

Description

Preparation of composite double base propellants This invention is concerned with the preparation of composite double base propellants by the in situ casting method, and with the propellants so obtained.
The in situ casting method for making double base propellants comprises placing a base powder comprising nitrocellulose and a stabiliser and, optionally, a nitric ester, an oxidizing and/or reducing solid charge, and/or a combustion catalyst system, into a mould, introducing a casting solvent comprising a nitric ester, a plasticiser, and a stabiliser,into the mould, and then curing the mixture, normally at an elevated temperature.
This method is briefly described, and contrasted with the alternative method of making double base propellants known as the "scurry casting" or "global" method, in U.S. Patent 4,080,411.
There is a requirement to improve the mechanical properties of double base propellants made by the in situ casting method, particularly those which are highly plasticised and which include inorganic or organic charges.
Double base propellants may be made in two different physical forms: (i) so-called "moulded-bonded" charges in which the propellant is in the form of a unitary moulded block.
Such compositions must be highly plasticised and in this case the purpose of improving the mechanical properties is to enhance the maximum stress (Sm) which the propellant can withstand in the hot state, while retaining a high maximum elongation (Em) in the cold state. Increasing the degree of plasticisation of such propellants improves their ballistic performance (specific pulse, volume specific pulse); for example in a typical composition the replacement of 5% of nitrocellulose in the base powder by 5% of nitroglycerin (which acts as a plasticiser) increases the specific pulse by 2 sec.
(ii) free grains. In this case, the purpose of improving the mechanical properties is to enhance mechanical strength in the hot state.
We have now found that the mechanical properties of double base propellants made by the in situ casting method can be substantially improved by introducing at least one polyisocyanate crosslinking agent into the base powder together with the casting solvent.
According to the present invention, therefore, there is provided a process of preparing a composite double base propellant by the in situ casting method, in which at least one polyisocyanate crosslinking agent is introduced together with the casting solvent into the base powder.
The polyisocyanate crosslinking agent may be added to the casting solvent simultaneously with the introduction of the latter into the mould containing the base powder, or it may be mixed with the casting solvent prior to the introduction of the latter. In both cases, it is important that the casting solvent should be substantially water-free; in particular, it is preferred that the casting solvent should contain less than 0.1% by weight of water. If a mixture of the casting solvent and the polyisocyanate crosslinking agent is to be stored for any length of time prior to use, it is necessary to take rigorous precautions to protect the mixture from any source of moisture.
As already mentioned, casting solvents for use in the in situ casting method comprise a nitric ester, for example, nitroglycerin, trimethylolethane trinitrate (TMETN), triethyleneglycol dinitrate (TRENo), 1,2,4- butanetriol trinitrate (BTTN), or propanediol dinitrate, or a mixture of two or more thereof (of which nitroglycerine is preferred); a non-energetic plasticiser, for example triacetin; and a stabiliser, for example 2-nitro-diphenylamine (2-NDPA), Centralite or N-methylpara-nitroaniline. The preferred casting solvent compositions are within the following ranges, by weight: nitric ester 72 to 83% non-energetic plasticiser 27.5 to 16% stabilizer 0.5 to 1% Nitrocellulose includes a number of free hydroxyl groups and it is with such hydroxyl groups that the isocynanate functions react.
Depending on the results required, the quantity of polyisocyanate to be added to the casting solvent, and thus finally to be incorporated in the propellant, is directly related to the quantity of nitrocellulose present in the base powder. It is preferred to use such a quantity of polyisocyanate that the ratio of NC0 groups to free OH equivalents present in the nitrocellulose is from 0.015 to 0.2, and more preferably from 0.03 to 0.15.
It is generally preferred to use bi-functional polyisocyanates, but polyisocyanates of higher functionality can also be used. Suitable diisocyanates include, for example, 2,4- and 2,6-toluene-diisocyanate (TDI), 1-methyl-2,4- and 2,6-cyclohexane-diisocyanate, 4,4'dicyclohexylmethane-diisocyanate, isophorone-diisocyanate, 1,6-hexane-diisocyanate (HMDI), 2,2,4-trimethyl-1,6-hexanediisocyanate, the base adducts of, for example, 1,6-hexanediisocyanate and their mixtures, 4,4',4"-triphenyl- methane-triisocyanate, and the adduct of 1,1 ,1-tri- hydroxymethylpropane and 1,6-hexane-diisocyanate.
Aliphatic diisocyanates are generally preferred because of their lower reaction rates to aromatic diisocyanates, but the latter may be used either alone or in admixture with aromatic diisocyanates.
When moulded-bonded propellants are made by the process of the invention, the degree of plasticisation can be increased (as compared with otherwise similar compositions not made with a polyisocyanate) while still obtaining the same, or even improved, mechanical properties. By this means, the energetic level of the propellant can be improved (by using nitroglycerine to increase the degree of plasticisation).
According to an optional feature of the invention, a prepolymer having hydroxyl terminations is incorporated in the base powder. Such an addition substantially improves the elongation of the product, in the cold, without substantially changing the maximum stress in the hot state. This modification is particularly advantageous in the production of moulded-bonded propellants.
The degree of plasticisation referred to herein means the following ratio, by weight, expressed as a percentage: nitroglycerin + non-energetic plasticiser nitroglycerin + non-energetic plasticiser + nitro cellulose + prepolymer (if present) The degree of plasticisation can be varied by varying the proportion of nitrocellulose in the base powder and/or by varying the proportion of casting solvent, the latter being determined by the mass filling coefficient (Rm %) required.
The mass filling coefficient is given by the following ratio: mass of base powder Rm(%) = mass of propellant Propellants having a degree of plasticisation as high as 88% can be obtained by the process of the invention.
The addition of a hydroxyl-terminated prepolymer to the base powder reduces the degree of plasticisation, so that if a high degree of plasticisation is required, the proportions of the other relevant constituents must be adjusted. The proportion of hydroxyl-terminated prepolymer, when used, is preferably not more than 5% by weight in order that the propellant should retain good ballistic properties. Preferred prepolymers for this purpose are those based on polyesters and polyethers.
The propellants made by the process of the invention preferably contain a high proportion of oxidizing charges, the latter preferably being nitramines, such as hexogen and octogen or mixtures thereof. The proportion of nitramine may be very high, up to 70% based on the weight of the base powder, subject, of course, to a corresponding adjustment of the nitric ester content so that the degree of plasticisation is not greater than 88%.
In order that propellants containing nitramine should show good ballistic performance, particularly a small pressure exponent, it is preferred that the base powder of such propellants should include combustion catalysts.
We have found that the use of lead inorganic salts for this purpose gives propellants with less satisfactory characteristics when an aromatic polyisocyanate is used in the process of the invention. On the other hand, excellent results are obtained with catalyst systems which comprise, based on the weight of the base powder: (a) 2 to 5% of a lead aromatic acid salt; (b) 1 to 4% of a copper aliphatic or aromatic acid salt, a lead aliphatic acid salt, or a copper oxide; (c) 0.05 to 2% of acetylene black (NA) or benzene black.
Suitable lead salts (a) include, for example, lead salicylate, lead 9-resorcylate, lead 2,5dihydroxybenzoate, and lead 2,4,6-trihydroxy-benzoate.
Suitable copper and lead salts (b) include, for example, copper or lead 2-ethyl-hexanoate, copper or lead octoate, dibasic copper or lead stearate, and copper salts of the aromatic acids mentioned under (a).
Preferred copper oxides (b) are cuprous oxide and cupric oxide.
The total amount of the catalyst system is preferably less than 10% , based on the weight of the base powder.
The base powder may, if desired, contain one or more anti-instability additives and these do not influence the crosslinking process. Such additives are often desirable in order to improve the combustion stability of the propellant and their not having any deleterious effect on the crosslinking is therefore very important.
In order that the invention may be more fully understood, the following examples are given by way of illustration only.
In these Examples (except Example 6), the casting solvent used had the following composition, by weight: nitroglycerin 78% triacetin 21% 2-NDPA 1% A quantity of the polyisocyanate identified in the Examples was added to this casting solvent so that the NCO/OH ratio in the final mixture was as shown below.
The method of making the propellant was in each case as follows. The casting solvent, with the polyisocyanate addition, was injected into the lower section of a mould containing the base powder and gelatinisation took place. The gelatinised mixture was cured at about 40"C for a few hours and then baked at from 600 to 650C for a few days, or was subjected to a continuous baking phase.
The base powder compositions specified in the Examples all additionally included 2% by weight of 2 -NDPA.
The mechanical properties of the resulting propellants were tested and their maximum stresses (Sm) are reported in MPa and their maximum elongations (Em) as %ages.
Example 1 Base powder Nitrocellulose 21.5 Nitroglycerin 25 Hexogen or octogen 45 Lead B-resorcylate 3 Copper octoate 2 NA 1.5 The mass filling coefficient (Rm%) was 69% and the NCO/OH ratio was 0.05 (that is, it was necessary to add approximately 0.4 part of diisocyanate to the casting solvent to obtain this NCO/OH ratio). The degree of plasticisation was 76.4%.
The results of testing are given in the table below:
DIISOCYANATE NITRAMINE Sm at 6o0C j Em at-400C I Hexogen 0.4 19 TDI Octogen 0.5 14 Hexogen ,6 18 HMDI Octogen i 0.6 19 Similar compositions, with octogen or hexogen, but without addition of polyisocyanate to the casting solvent, had no detectable Sm at + 600 C.
Example 2 The base powder was the octogen-containing composition of Example 1. Using different amounts of polyisocyanate to give different NCO/OH ratios, the results obtained were as follows:
NCO/OH Sm at 60?C j Em at -400C 0.5 0.6 1 19 0.075 0.6 1 18 0.094 0.5 15 Example 3 The base powder of Example 1 was used, except that 3% by weight of a polyether-polyester prepolymer having hydroxyl terminations was added. The crosslinking agent was HMDI.
The NCO/OH ratio was 0.09,the filling coefficient was 69%, and the degree of plasticisation was 76.4%.
The test results of the resulting propellant were: Sm at +600C, 0.4; Em at -400C, 30.
Example 4 Base powder Nitrocellulose 16.5 Nitroglycerin 30 Hexogen 45 Lead p-resorcylate 3 Copper octoate 2 NA 1.5 The diisocyanate used was HMDI, the NCO/OH ratio was 0.05, the filling coefficient was 68,and the degree of plasticisation was 82.3%. The test results were: Sm at +600C, 0.4; Em at -400C, 40; at -50 C, 20.
Example 5 Base powder Nitrocellulose 21.5 Nitroglycerin 20 Hexogen 50 Lead p-resorcylate 3 Copper octoate 2 NA 1.5 The diisocyanate was HMDI, the NCO/OH ratio was 0.06, the filling coefficient was 72%, and the degree of plasticisation was 73.3%. The test results were: Sm at +600C, 0.5; Em at -400C, 10.
Example 6 The composition of the casting solvent, by weight, was as follows: Nitroglycerin 81.5% Triacetin 17.5% 2-NDPA 1 % The base powder composition, by weight, was Nitrocellulose 11% Nitroglycerin 25% Hexogen 55% Lead -resorcylate 3% Cupric oxide 2% NA 1.5% The diisocyanate used was HMDI, the NCO/OH ratio was 0.08, the mass filling coefficient was 72%, and the degree of plasticisation was 84%. The mechanical characteristics of the propellant obtained were: Sm at 600C, 0.6; Em at -400C, 30.
Example 7 Front combustion propellants 90 mm in diameter and 90 mm in length and prepared as described in Example 1 were fired as boosters. The firing results are shown in Figures 1 and 2 of the accompanying drawing in which combustion rate (Vc) is plotted against combustion pressure (P).
Figure 1 was obtained with a propellant in which the isocyanate was HMDI and the nitramine was hexogen, and Figure 2 with a propellant obtained with the same isocyanate and with octogen as the nitramine.

Claims (16)

Claims:
1. A process of preparing a composite double base propellant by the in situ casting method, in which at least one polyisocyanate crosslinking agent is introduced together with the casting solvent into the base powder.
2. A process according to claim 1, in which the amount of polyisocyanate crosslinking agent is such that the ratio of NCO to free OH equivalents in the nitrocellulose of the base powder is from 0.015 to 0.2.
3. A process according to claim 2, in which said NCO/OH ratio is from 0.03 to 0.15.
4. A process according to any of claims 1 to 3, in which the crosslinking agent is a diisocyanate.
5. A process according to any of claims 1 to 4, in which the crosslinking agent is an aliphatic diisocyanate.
6. A process according to any of claims 1 to 5, in which the degree of plasticisation of the propellant obtained is up to 88%.
7. A process according to any of claims 1 to 6, in which the base powder contains up to 5% by weight of a prepolymer having hydroxyl terminations.
8. A process according to claim 7, in which the prepolymer is a polyester or a polyether.
9. A process according to any of claims 1 to 8 in which the base powder contains a solid oxidising charge.
10. A process according to claim 9, in which the oxidising charge is a nitramine.
11. A process according to claim 10, in which the nitramine is hexogen or octogen of a mixture thereof.
12. A process according to claim 10 or 11, in which the base powder contains up to 70% by weight of the nitramine.
13. A process according to any of claims 1 to 12, in which the base powder contains up to 10% by weight of combustion catalysts.
14. A process according to any of claims 1 to 13, in which the base powder contains one or more antiinstability additives.
15. Composite double base propellants when made by the process claimed in any of the preceding claims.
15. A process of preparing a composite double base propellant according to claim 1, substantially as herein described in any of Examples 1 to 6
16. Composite double base propellants when made by the process claimed in any of the preceding claims.
Amendments to the claims have been filed as follows 1. A process of preparing a composite double base propellant by the in situ casting method. in which at least one polyisocyanate crosslinking agent is introduced together with the casting solvent into the base powder, the amount of the crosslinking agent being such that the ratio of NCO to free OH equivalents in the nitrocellulose of the base powder is fro 0.015 to 0 n.s.
2. A process according to claim 1, in which said NCO/OH ratio is from 0.03 to 0.15.
3. A process according to claim 1 or 2, in which the crosslinking agent is a diisocyanate.
4. A process according to any of claims 1 to 3, in which the crosslinking agent is an aliphatic diisocyanate.
5. A process according to any of claims 1 to 4, in which the degree of plasticisation (as herein defined) of the propellant obtained is up to s8.
6. A process according to any of claims 1 to 5, in which the base powder contains up to 5% by weight of a prepolymer having hydroxyl terminations.
7. A process according to claim 6, in which the prepolymer is a polyester or a polyether.
8. A process according to any of claims 1 to 7 in which the base powder contains a solid oxidising charge.
9. A process according to claim 8, in which the oxidising charge is a nitramine.
10. A process according to claim 9, in which the nitramine is hexogen or octogen or a mixture thereof.
11. A process according to claim 9 or 10, in which the base powder contains up to 70% by weight of the nitramine.
12. A process according to any of claims 1 to 11, in which the base powder contains up to 10% by weight of combustion catalysts.
13. A process according to any of claims 1 to 12, in which the base powder contains one or more antiinstability additives.
14. A process of preparing a composite double base propellant according to claim 1, substantially as herein described in any of Examples 1 to 6.
GB8413649A 1983-06-30 1984-05-29 Preparation of composite double base propellants Expired - Fee Related GB2257968B (en)

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
FR8310834A FR2680783B1 (en) 1983-06-30 1983-06-30 PROCESS FOR IMPROVING THE MECHANICAL PROPERTIES OF A DOUBLE COMPOSITE BASED PROPERGOL OBTAINED BY THE MOLDING METHOD AND PROPERGOL THUS OBTAINED.

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GB8413649D0 GB8413649D0 (en) 1992-11-18
GB2257968A true GB2257968A (en) 1993-01-27
GB2257968B GB2257968B (en) 1993-10-13

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DE (1) DE3420906C2 (en)
FR (1) FR2680783B1 (en)
GB (1) GB2257968B (en)
IT (1) IT1238359B (en)

Families Citing this family (1)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
GB8409867D0 (en) * 1984-04-16 1993-06-16 Ici Plc Nitrocellulose propellant composition

Citations (4)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
GB1408554A (en) * 1966-09-01 1975-10-01 Us Navy Crosslinking of double base propellants
GB1427697A (en) * 1969-08-12 1976-03-10 Hercules Inc Process for producing cross-linked propellants
GB1447025A (en) * 1966-10-14 1976-08-25 Us Navy Solution cast double base propellants
GB1588605A (en) * 1978-02-01 1981-04-29 Hercules Inc Method of preparing slurry-cast propellant

Family Cites Families (6)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
US4029529A (en) * 1967-07-12 1977-06-14 The United States Of America As Represented By The Secretary Of The Navy Crosslinked carboxyl containing polymer and nitrocellulose as solid propellant binder
US4080411A (en) * 1968-08-21 1978-03-21 Hercules Incorporated Slurry-cast propellant method
US3798090A (en) * 1968-12-04 1974-03-19 Hercules Inc Process for producing cross-linked propellants
US4234364A (en) * 1978-05-30 1980-11-18 Hercules Incorporated Crosslinked double base propellant binders
CA1154260A (en) * 1979-12-28 1983-09-27 Alliant Techsystems Inc. Slurry cast double base propellants
GB2092563B (en) * 1981-02-10 1984-05-02 Hercules Inc Alkoxy substituted aromatic stabilisers for cross-linked cmdb propellants

Patent Citations (4)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
GB1408554A (en) * 1966-09-01 1975-10-01 Us Navy Crosslinking of double base propellants
GB1447025A (en) * 1966-10-14 1976-08-25 Us Navy Solution cast double base propellants
GB1427697A (en) * 1969-08-12 1976-03-10 Hercules Inc Process for producing cross-linked propellants
GB1588605A (en) * 1978-02-01 1981-04-29 Hercules Inc Method of preparing slurry-cast propellant

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Publication number Publication date
GB2257968B (en) 1993-10-13
DE3420906A1 (en) 1993-05-19
FR2680783B1 (en) 1994-05-06
DE3420906C2 (en) 1996-02-29
IT8467650A0 (en) 1984-06-27
IT1238359B (en) 1993-07-13
GB8413649D0 (en) 1992-11-18
FR2680783A1 (en) 1993-03-05

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