US2858289A - Combustion inhibitor for gas-producing charges - Google Patents
Combustion inhibitor for gas-producing charges Download PDFInfo
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- US2858289A US2858289A US357384A US35738453A US2858289A US 2858289 A US2858289 A US 2858289A US 357384 A US357384 A US 357384A US 35738453 A US35738453 A US 35738453A US 2858289 A US2858289 A US 2858289A
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Classifications
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- F—MECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
- F42—AMMUNITION; BLASTING
- F42B—EXPLOSIVE CHARGES, e.g. FOR BLASTING, FIREWORKS, AMMUNITION
- F42B5/00—Cartridge ammunition, e.g. separately-loaded propellant charges
- F42B5/02—Cartridges, i.e. cases with charge and missile
- F42B5/18—Caseless ammunition; Cartridges having combustible cases
- F42B5/192—Cartridge cases characterised by the material of the casing wall
- F42B5/196—Coatings
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- C—CHEMISTRY; METALLURGY
- C06—EXPLOSIVES; MATCHES
- C06B—EXPLOSIVES OR THERMIC COMPOSITIONS; MANUFACTURE THEREOF; USE OF SINGLE SUBSTANCES AS EXPLOSIVES
- C06B23/00—Compositions characterised by non-explosive or non-thermic constituents
- C06B23/007—Ballistic modifiers, burning rate catalysts, burning rate depressing agents, e.g. for gas generating
-
- C—CHEMISTRY; METALLURGY
- C06—EXPLOSIVES; MATCHES
- C06B—EXPLOSIVES OR THERMIC COMPOSITIONS; MANUFACTURE THEREOF; USE OF SINGLE SUBSTANCES AS EXPLOSIVES
- C06B45/00—Compositions or products which are defined by structure or arrangement of component of product
- C06B45/04—Compositions 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
- C06B45/06—Compositions 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
- C06B45/10—Compositions 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
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- C—CHEMISTRY; METALLURGY
- C08—ORGANIC MACROMOLECULAR COMPOUNDS; THEIR PREPARATION OR CHEMICAL WORKING-UP; COMPOSITIONS BASED THEREON
- C08F—MACROMOLECULAR COMPOUNDS OBTAINED BY REACTIONS ONLY INVOLVING CARBON-TO-CARBON UNSATURATED BONDS
- C08F259/00—Macromolecular compounds obtained by polymerising monomers on to polymers of halogen containing monomers as defined in group C08F14/00
- C08F259/02—Macromolecular compounds obtained by polymerising monomers on to polymers of halogen containing monomers as defined in group C08F14/00 on to polymers containing chlorine
- C08F259/04—Macromolecular compounds obtained by polymerising monomers on to polymers of halogen containing monomers as defined in group C08F14/00 on to polymers containing chlorine on to polymers of vinyl chloride
-
- C—CHEMISTRY; METALLURGY
- C08—ORGANIC MACROMOLECULAR COMPOUNDS; THEIR PREPARATION OR CHEMICAL WORKING-UP; COMPOSITIONS BASED THEREON
- C08F—MACROMOLECULAR COMPOUNDS OBTAINED BY REACTIONS ONLY INVOLVING CARBON-TO-CARBON UNSATURATED BONDS
- C08F265/00—Macromolecular compounds obtained by polymerising monomers on to polymers of unsaturated monocarboxylic acids or derivatives thereof as defined in group C08F20/00
- C08F265/04—Macromolecular compounds obtained by polymerising monomers on to polymers of unsaturated monocarboxylic acids or derivatives thereof as defined in group C08F20/00 on to polymers of esters
- C08F265/06—Polymerisation of acrylate or methacrylate esters on to polymers thereof
-
- C—CHEMISTRY; METALLURGY
- C08—ORGANIC MACROMOLECULAR COMPOUNDS; THEIR PREPARATION OR CHEMICAL WORKING-UP; COMPOSITIONS BASED THEREON
- C08K—Use of inorganic or non-macromolecular organic substances as compounding ingredients
- C08K5/00—Use of organic ingredients
- C08K5/0008—Organic ingredients according to more than one of the "one dot" groups of C08K5/01 - C08K5/59
- C08K5/0016—Plasticisers
-
- C—CHEMISTRY; METALLURGY
- C08—ORGANIC MACROMOLECULAR COMPOUNDS; THEIR PREPARATION OR CHEMICAL WORKING-UP; COMPOSITIONS BASED THEREON
- C08K—Use of inorganic or non-macromolecular organic substances as compounding ingredients
- C08K5/00—Use of organic ingredients
- C08K5/04—Oxygen-containing compounds
- C08K5/10—Esters; Ether-esters
- C08K5/11—Esters; Ether-esters of acyclic polycarboxylic acids
-
- C—CHEMISTRY; METALLURGY
- C08—ORGANIC MACROMOLECULAR COMPOUNDS; THEIR PREPARATION OR CHEMICAL WORKING-UP; COMPOSITIONS BASED THEREON
- C08L—COMPOSITIONS OF MACROMOLECULAR COMPOUNDS
- C08L27/00—Compositions of homopolymers or copolymers of compounds having one or more unsaturated aliphatic radicals, each having only one carbon-to-carbon double bond, and at least one being terminated by a halogen; Compositions of derivatives of such polymers
- C08L27/02—Compositions of homopolymers or copolymers of compounds having one or more unsaturated aliphatic radicals, each having only one carbon-to-carbon double bond, and at least one being terminated by a halogen; Compositions of derivatives of such polymers not modified by chemical after-treatment
- C08L27/04—Compositions of homopolymers or copolymers of compounds having one or more unsaturated aliphatic radicals, each having only one carbon-to-carbon double bond, and at least one being terminated by a halogen; Compositions of derivatives of such polymers not modified by chemical after-treatment containing chlorine atoms
- C08L27/06—Homopolymers or copolymers of vinyl chloride
-
- C—CHEMISTRY; METALLURGY
- C08—ORGANIC MACROMOLECULAR COMPOUNDS; THEIR PREPARATION OR CHEMICAL WORKING-UP; COMPOSITIONS BASED THEREON
- C08L—COMPOSITIONS OF MACROMOLECULAR COMPOUNDS
- C08L33/00—Compositions of homopolymers or copolymers of compounds having one or more unsaturated aliphatic radicals, each having only one carbon-to-carbon double bond, and only one being terminated by only one carboxyl radical, or of salts, anhydrides, esters, amides, imides or nitriles thereof; Compositions of derivatives of such polymers
- C08L33/04—Homopolymers or copolymers of esters
- C08L33/06—Homopolymers or copolymers of esters of esters containing only carbon, hydrogen and oxygen, which oxygen atoms are present only as part of the carboxyl radical
- C08L33/10—Homopolymers or copolymers of methacrylic acid esters
- C08L33/12—Homopolymers or copolymers of methyl methacrylate
Definitions
- This invention relates to gas-producing charges having surfaces which are inhibited or restricted from burning and to plastic inhibitor compositions for this purpose.
- the most desirable inhibitor has been found to be cellulose acetate.
- Cellulose acetate has been-applied to grains of gas-producing compositions and in particular to rocket grains of double-base smokeless powder in many ways. Initially the grains were inhibited by cementing plastic patches to the surface or applying a convolute wrapping of cellulose acetate sheet material suitably moistened with anadhesion promoting agent such as acetone or by suitable adhesive composition.
- anadhesion promoting agent such as acetone or by suitable adhesive composition.
- the inhibitor structures were preformed and, in accordance with one procedure, the gas-producing charge is cast directly into preformed cylindrical cellulose acetate tubes.
- the charge is initially prepared by casting or extrusion and then fitted into a hollow cylinder of cellulose acetate which had been prepared by wrapping or extrusion. Restriction of end surfaces has usually been achieved by bonding preformed plates to the desired portions of the grain ends.
- cellulose acetate inhibitor and inhibitors made of similar materials such as ethyl cellulose have been reasonably satisfactory and have contributed greatly to the development of improved gas-producing charges.
- ethyl cellulose has been reasonably satisfactory and have contributed greatly to the development of improved gas-producing charges.
- Probably one of the most serious faults of cellulose acetate is found in the fact that when the usual double-base smokeless powder grain is restricted with this plastic material, an undesirably large amount of nitroglycerin migrates from the powder grain into the inhibitor during storage. Of probably equal seriousness is the migration of plasticizer from the inhibitor layer into the base grains.
- plastic compositions may be prepared and gas-producing charges: may be fabricated employing such plastic compositions; which are characterized by greatly improved properties.
- compositions of the invention will form excellent? bonds with gas-producing charges, particularly those con-- taining nitrocellulose, without detrimental migration of? explosive plasticizer from the gas-producing grain.
- the present invention is a gasproducing charge comprising a body of combustible gasproducing composition having at least part of its surface:
- the gas-producing charge is: preferably a smokeless powder composition and may bea single base formulation comprising nitrocellulose, but?
- Thegas-producing charge may also be formed from other combustible materials currently employed by the art' such as ammonium nitrate and nitroguanidine which may be compacted into suitable physical form with or without the use of a binding agent or matrix suchas nitrocellulose or various synthetic resins;
- Thegas-producing charge may have any desired configuration but in accordance withcurrent practiceis normally a cylindrical grain having its outer cylindrical surface inhibited from burning in accordance with the invention.
- An inhibitor layer may also be employed on either or both ends of the grain depending upon the internal geometry of the grain. In some embodiments, such as in perforated grains, it is desirable to inhibit the outer surface and perforation surface and allow only end burning.
- the cured and uncured'inhibitor compositions comprising from 25 to 50% monomeric butyl methacrylate, from 25 to 45% of a copolymer of vinyl chloride with not more than about 5% of vinyl acetate, from 5 to 30% of polymeric methyl methacrylate, and 5 to 20% of a nonvolatile plasticizer for the vinyl chloride-vinyl acetate copolymer.
- amounts up to and including 15% of a bifunctional cross-linking monomer may also be included in the composition.
- the most desirable bifunctional cross-linking monomer is the dimethacrylate of polyethylene glycol 200 (BCM). Improved results have also been obtained with divinyl benzene, although some bond failures after extended storage at 66% C. have still been encountered. With BCM, on the'other hand, excellent results are still obtained at such temperatures.
- butyl methacrylate normally results in bond failure during storage, while the use of more than 50 parts of butyl methacrylate monomer results in a mixture which allows the polymeric constituents of the composition, and particularly the polymethyl methacrylate, to settle out prior to curing. Furthermore, when a composition containing more than 50 parts of butyl methacrylate monomer is employed, the resulting cured product becomes brittle with resulting bond failure and cracking of the restriction during curing, storage, and temperature cycling.
- polymethyl methacrylate The presence of at least 5% polymethyl methacrylate is essential to the formation of a satisfactory bond. However, if more than 30% of polymethyl methacrylate is employed, bond failures are again obtained during storage.
- a plasticizer for the vinyl chloride-vinyl acetate copolymer is essential to a composition which does not become so brittle upon curing that the bond between the powder grain and the inhibitor is destroyed.
- plasticizer if more than 20 parts of plasticizer is employed, the resistance of the inhibitor to nitroglycerin absorption is again lowered and failure of the inhibitor itself is 'usually obtained in storage.
- the incorporation of the bifunctional cross-linking monomer is optional depending upon the use to which the restricted gas-producing charges are to be put. It is preferred, however, that the cross-linking agent be employed in all compositions since its presence has been found to preserve the integrity of the bond between the gas-producing charge and the inhibitor under all temperature conditions which can reasonably be expected even during military operations.
- the cross-linking obtained by the incorporation of the cross-linking agent does cause a hard ening of the inhibitor.
- the amount of hardening obtained is not disadvantageous as long as not more than 15 parts of the cross-linking agent is employed. When more than 15 parts is'employed, undesirable brittleness of the cured product is obtained with resulting bond faliures.
- the inhibitor compositions in accordance with the invention cure rapidly with conventional polymerization catalysts for acrylic compounds and at low temperatures. Cure time depends on the thickness of the restriction layer and the type and amount of catalyst.
- Examples l31 are included to demonstrate operable inhibitor compositions and to illustrate the necessity of observing the limitations above set forth.
- Each of the compositions set forth was applied to a cylindrical grain of double-base smokeless powder containing nitroglycerin by concentrically disposing the powder grain in an oversized cylindrical mold equipped with a steam jacket and filling the resulting annulus between grain and mold with the uncured mix. The composition was cured for about one hour at a temperature of C. After removal from the mold, the restriction and bond were examined. The inhibited grains were then placed in hot storage and unless otherwise indicated, were maintained at about 60 C. for a period of three weeks and examined at weekly intervals. forth in-Table -1 under Remarks. 'All the compositions in Table 1 contained about 4% of Luperco ATC (a 50:50 mixture of benzoyl peroxide and tricresyl phos phate) as a polymerization catalyst.
- Luperco ATC a 50:50 mixture of benzoyl peroxide and
- Examples 32-37 are presented to illustrate the criticality of the 95/5 ratio of PVC/PVA.
- Thirty (30) percent of the PVC-PVA copolymer was employed 5 DVB (18%)--- 10 DVB (18%) 1o DVB 45% 5 DvB 45% 10 BCM in 2111 cases.
- the commercial designation of the polymer 40 employed is set forth in parenthesis.
- the inhibitor was applied to double-base smokeless powder grains by the bond good (in hot storage the plastic softened undesirably).
- good bond-good plastic satisfactory bondplastic satisfactory but softened somewhat in hot storage.
- satisfactory bond-plastic satisfactory but becoming brittleuncured mix thin and some PMMA settled out while standing.
- bond failed in hot storageplastic satisfactory -uncured mix was very thin allowing the PMMA to settle out.
- outer surfaces of the remaining groups were restricted in accordance with the invention.
- the outer surfaces of group 2 were restricted by casting around the grains a mix containing 40% monomeric butyl methacrylate,
- Catalyst-Luperco ATO (/50 benzoyl peroxide) tricrcsyl phosphate.
- Example 38 Four groups of solid, cylindrical, end-burning grains were prepared. The outer surfaces of group 1 were con- 60 C. storage for 36 weeks and at the end of each week a grain from each group was removed and its restriction analyzed to determine nitroglycerin absorption. In the analysis the standard TiCl method on a methylene chloride extract was employed. At the end of 12 weeks the cellulose acetate restriction contained 29% by weight ventionally restricted with cellulose acetate, while the of nitroglycerin. At the end of 12 weeks it was noted that nitroglycerin absorption had practically leveled off in all the restrictions. At the end of 36 weeks, the restrictions of groups 2, 3, and 4 contained a maximum of 8%, and 7.5%, respectively.
- Example 39 Restricted grains similar to those of groups 2, 3, and 4 were placed in 80 C. storage for 9 weeks. Bond failures occured in group 2 at the end of two days. At the end of 9 weeks plastic and bonds in groups 3 and 4 were oxide is especially preferred in view of the low temperature necessary to effect polymerization with this material.
- a filler material in the restriction composition such as glass wool, asbestos fioc, and the like.
- the plastic inhibitor compositions of the invention may be applied to external or perforation surfaces of gasproducing charges in any desired manner.
- the preferred method is to place an unrestricted grain into an oversized mold and then introduce the curable mix or slurry into the annulus around the grain in such a manner as to prevent entrapment of air. This is best accomplished by introducing the mix under pressure into the base of the mold. The entire mold is then subjected to curing conditions until the plastic has set and a bond has been formed.
- Perforation surfaces may be similarly inhibited by employing undersized forms and then introducing the uncured mix into the space between form and perforation surface.
- the plastic inhibitor may be initially molded and the propellant grain subsequently cast in the hollow inhibitor cylinder, thus using this cylinder as a mold or casting container. A satisfactory bond is obtained between inhibitor and grain during the curing of the grain.
- Another operable method is to separately prefabricate both the inhibitor and the grain to close tolerances, apply a mutual solvent to the surface of the grain, and then slide the grain into the inhibitor cylinder.
- the inhibitor is especially preferred, however, to cast the inhibitor around the finished grain or in a perforation, since it is by this procedure that the best bond is obtained.
- the enhanced bond thus produced results from the solvent action of the monomeric butyl methacrylate monomer on the nitrocellulose on the surface of the gas-producing grain. Since the butyl methacrylate is also a solvent for the polymeric constituents of the inhibitor, the nitrocellulose polymer and the polyvinyl chloride acetatepolymethyl methacrylate of the inhibitor are held in mutual solution at the surface of the grain. Thus, when the butyl methacrylate is polymerized, a strong bond is obtained. The strength of this bond and the ruggedness of the inhibitor composition as a whole is further enhanced by cross-linking of the butyl methacrylate when the bifunctional cross-linking monomer such as BCM or divinylbenzene is employed.
- any of the conventional plasticizers for PVC-A employed by the art are operable when employed in the critical amount.
- tricresyl phosphate is preferred in view of its plasticizing properties and further in view of its fireproofing effect on the composition.
- Other plasticizers which may be employed include, without limitation, diallyl phthalate, trioctyl phthalate, trioctyl phosphate, dibutyl sebacate, and dibutyl adipate.
- polymerization catalysts for acrylic monomers are known to the art and may be employed in place of any of the catalysts illustrated by the examples.
- Such materials include lauroyl peroxide, di-tert-butyl peroxide, tertiary butyl hydroperoxide, cumene hydroperoxide, methyl ethyl ketone peroxide, and tertiary butyl perbenzoate.
- the operable catalysts those of the peroxide type are the most desirable. Benzoyl perthe appended claims.
- a curable mixture adapted for inhibitor application to combustible gas-producing charges comprising by weight from 25 to 50% monomeric butyl methacrylate, from 25 to 45% of a copolymer of vinyl chloride with not more than about 5% of vinyl acetate, from 5 to 30% of polymeric methyl methacrylate, and from 5 to 20% of a nonvolatile plasticizer for the vinyl chloride-vinyl acetate copolymer.
- a curable mixture adapted for inhibitor application to combustible gas-producing charges comprising by weight from 25to 50% monomeric butyl methacrylate, from 25 to 45 of a copolymer of vinyl chloride with not more than about 5% of vinyl acetate, from 5 t6 30% of polymeric methyl methacrylate, an amount not exceeding 15% of the dimethacrylate of ethylene glycol,
- a composition of matter comprising the cured product of a mixture containing from 25 to 50% monomeric butyl methacrylate, from 25 to 45 of a copolymer of vinyl chloride with not more than about 5% of vinyl acetate, from 5 to 30% of polymeric methyl methacrylate, and from 5 to 20% of a nonvolatile plasticizer for-the vinyl chloride-vinyl acetate copolymer, said product being adapted for inhibitor application to a combustible gasproducing charge.
- composition according to claim 7 in which the plasticizer is tricresyl phosphate.
- a composition of matter comprising the cured product of a mixture containing from 25 to 50% monom'er ic butyl methacrylate, from 25 to 45 of a copolymer of vinyl chloride with not more than about 5% of vinyl acetate, from 5 to 30% of polymeric methyl methacrylate, an amount not exceeding 15 of the dimethacrylate of ethylene glycol, and from 5 to 20% of a nonvolatile plasticizer for the vinyl chloride-vinyl acetate copolymer, said product being adapted for inhibitor application to a combustible gas-producing charge.
- composition according to claim 9 in which the plasticizer is tricresyl phosphate.
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Description
United States PatetitO COMBUSTION INHIBITOR FOR GAS-PRODUCING CHARGES James N. Bohn, Kenvil, N. 1., and Allan G. Sandholf,
Cumberland, Md., assignors to Hercules Powder Company, Wilmington, DeL, a corporation of Delaware No Drawing. Application May 25, 1953 Serial No. 357,384
Claims. (Cl. 26030.6)
This invention relates to gas-producing charges having surfaces which are inhibited or restricted from burning and to plastic inhibitor compositions for this purpose.
In the contemporary development of solid propellants, it has been found necessary to the attainment of desirable characteristics to inhibit some surfaces of the combustible gas-producing charges from burning. Up to the present time the most desirable inhibitor has been found to be cellulose acetate. Cellulose acetate has been-applied to grains of gas-producing compositions and in particular to rocket grains of double-base smokeless powder in many ways. Initially the grains were inhibited by cementing plastic patches to the surface or applying a convolute wrapping of cellulose acetate sheet material suitably moistened with anadhesion promoting agent such as acetone or by suitable adhesive composition. As the art developed, the inhibitor structures were preformed and, in accordance with one procedure, the gas-producing charge is cast directly into preformed cylindrical cellulose acetate tubes. In accordance with alternative methods, the charge is initially prepared by casting or extrusion and then fitted into a hollow cylinder of cellulose acetate which had been prepared by wrapping or extrusion. Restriction of end surfaces has usually been achieved by bonding preformed plates to the desired portions of the grain ends.
The cellulose acetate inhibitor and inhibitors made of similar materials such as ethyl cellulose have been reasonably satisfactory and have contributed greatly to the development of improved gas-producing charges. However, it has been recognized for several years that even the preferred cellulose acetate restriction left much to be desired. Probably one of the most serious faults of cellulose acetate is found in the fact that when the usual double-base smokeless powder grain is restricted with this plastic material, an undesirably large amount of nitroglycerin migrates from the powder grain into the inhibitor during storage. Of probably equal seriousness is the migration of plasticizer from the inhibitor layer into the base grains. Ballistically the two effects are additive, since loss of nitroglycerin from the grain and pick-up of cooling plasticizer by the grain lower the overall poten-' tial. This problem has not been a serious one where the powder grains were employed immediately or where the time of storage was short. However, it is evident that for military uses in particular, it is usually necessary to stockpile large numbers of such gas-producing grains under varying conditions of storage for long periods of time. For accuracy and optimum performance it is essential that the grains perform in substantially the same manner at the end of a storage period as at the beginning of the storage period. Depending upon the amount of nitroglycerin migration into the inhibitor, the characteristics of the grain necessarily change during storage. Due to the leaching of the nitroglycerin from the peripheral surface of the grain, the ballistics ofthe charge are changed cellulose acetate inhibitor, there has been a continuous r eifort on the part of the explosives art to develop a ma" and the grain structure ,itself becorries characterized by p 2,8582% Patented Oct. 28, s.
2 diiferent structural strengths and ignition characteristics depending upon the nitroglycerin content at a particular point. Furthermore, burning time is seriously affected by plasticizer migration. It is apparent that where the gas producing charge is employed as the sole means of propulsion of a guided missile such variations in the makeup and structural characteristics of the burning chargecan have serious ramifications with respect to accuracy' forced to thicker inhibitors, this is an undesirable ap--- proach to the problem, since for the same size rocket;
motor and a given propellant composition any increase: in the thickness of the inhibitor layer must necessarily work a proportional decrease in the amount of gas-producing .pay load.
In view of these recognized faults of even the preferredl terial for use as a restriction which will give the neces sary bond between the inhibitor and the gas-producing:
charge, which will not absorb nitroglycerin or other ex. plosive plasticizer in any substantial amount, and which,
will retain the necessary bonded relationship for the nec-- essary period of time even though subjected to varying: storage conditions in terms of temperature changes andl the like. This effort on the part of the art has been completely unsuccessful, however, and at the present time cel! lulose acetate, despite its known faults, is still considered to be the best available combustion inhibitor for most gas-producing charges.
Now in accordance with the present invention, plastic compositions may be prepared and gas-producing charges: may be fabricated employing such plastic compositions; which are characterized by greatly improved properties..
The compositions of the invention will form excellent? bonds with gas-producing charges, particularly those con-- taining nitrocellulose, without detrimental migration of? explosive plasticizer from the gas-producing grain.
Generally described, the present invention is a gasproducing charge comprising a body of combustible gasproducing composition having at least part of its surface:
covered by a burning inhibitor layer of plastic composition bonded thereto, said plastic composition comprising the cured product of a mixture containing from 25 to 50% monomeric butyl methacrylate, from 25 to 45%= of a finely-divided copolymer of vinyl chloride with not. more than about 5% of vinyl acetate, from 5 to 30% of finely-divided polymeric methyl methacrylate, and 5 to 20% of a nonvolatile plasticizer for the vinyl chloride-- vinyl acetate copolymer. The gas-producing charge is: preferably a smokeless powder composition and may bea single base formulation comprising nitrocellulose, but? will ordinarily be a double-base composition containingv nitrocellulose and nitroglycerin or similar explosive plas-- ticizer such as other liquid explosive nitric esters. Thegas-producing charge may also be formed from other combustible materials currently employed by the art' such as ammonium nitrate and nitroguanidine which may be compacted into suitable physical form with or without the use of a binding agent or matrix suchas nitrocellulose or various synthetic resins; Thegas-producing charge may have any desired configuration but in accordance withcurrent practiceis normally a cylindrical grain having its outer cylindrical surface inhibited from burning in accordance with the invention. An inhibitor layer may also be employed on either or both ends of the grain depending upon the internal geometry of the grain. In some embodiments, such as in perforated grains, it is desirable to inhibit the outer surface and perforation surface and allow only end burning.
Also included in the invention are the cured and uncured'inhibitor compositions comprising from 25 to 50% monomeric butyl methacrylate, from 25 to 45% of a copolymer of vinyl chloride with not more than about 5% of vinyl acetate, from 5 to 30% of polymeric methyl methacrylate, and 5 to 20% of a nonvolatile plasticizer for the vinyl chloride-vinyl acetate copolymer. In accordance with the invention and in order to obtain even stronger bonds which will survive repeated cycling from low to high temperature in storage, amounts up to and including 15% of a bifunctional cross-linking monomer may also be included in the composition. The most desirable bifunctional cross-linking monomer is the dimethacrylate of polyethylene glycol 200 (BCM). Improved results have also been obtained with divinyl benzene, although some bond failures after extended storage at 66% C. have still been encountered. With BCM, on the'other hand, excellent results are still obtained at such temperatures.
As will be illustrated in the subsequently presented examples, it has been found that the ranges of incorporation for the various constituents of the plastic inhibiting material of this invention are critical to obtaining a satisfactory inhibitor, particularly when the inhibitor is employed to restrict from burning surfaces of the usually employed smokeless powder charges comprising nitrocellulose and nitroglycerin.
The use of less than 25 parts of butyl methacrylate normally results in bond failure during storage, while the use of more than 50 parts of butyl methacrylate monomer results in a mixture which allows the polymeric constituents of the composition, and particularly the polymethyl methacrylate, to settle out prior to curing. Furthermore, when a composition containing more than 50 parts of butyl methacrylate monomer is employed, the resulting cured product becomes brittle with resulting bond failure and cracking of the restriction during curing, storage, and temperature cycling.
If less than 25 parts of polyvinyl chloride'acetate copolymer is employed, bond failure normally results and nitroglycerin is absorbed from a double-base gas-producing charge of smokeless powder. On the other hand, if more than 45 parts of the copolymer'are employed, the uncured mix rapidly becomes too viscous to handle satisfactorily and also prevents the formation of even a satisfactory initial powder-inhibitor bond. In addition, the increased viscosity makes it prohibitively difiicult to remove entrapped air from the uncured composition. Furthermore, it has been found that if the copolymer contains more than about 5% vinyl acetate, either the composition does not set up at all or else the bond fails even 4 at room temperature storage due to the softness of the composition.
The presence of at least 5% polymethyl methacrylate is essential to the formation of a satisfactory bond. However, if more than 30% of polymethyl methacrylate is employed, bond failures are again obtained during storage.
The presence of at least 5% of a plasticizer for the vinyl chloride-vinyl acetate copolymer is essential to a composition which does not become so brittle upon curing that the bond between the powder grain and the inhibitor is destroyed. However, if more than 20 parts of plasticizer is employed, the resistance of the inhibitor to nitroglycerin absorption is again lowered and failure of the inhibitor itself is 'usually obtained in storage.
The incorporation of the bifunctional cross-linking monomer is optional depending upon the use to which the restricted gas-producing charges are to be put. It is preferred, however, that the cross-linking agent be employed in all compositions since its presence has been found to preserve the integrity of the bond between the gas-producing charge and the inhibitor under all temperature conditions which can reasonably be expected even during military operations. The cross-linking obtained by the incorporation of the cross-linking agent does cause a hard ening of the inhibitor. However, the amount of hardening obtained is not disadvantageous as long as not more than 15 parts of the cross-linking agent is employed. When more than 15 parts is'employed, undesirable brittleness of the cured product is obtained with resulting bond faliures.
The inhibitor compositions in accordance with the invention cure rapidly with conventional polymerization catalysts for acrylic compounds and at low temperatures. Cure time depends on the thickness of the restriction layer and the type and amount of catalyst.
Having generally described the invention, the following examples are given in order to illustrate operable compositions and gas-producing charges and to illustrate the criticality of the proportions of the plastic inhibitor composition of the invention.
In Table 1, Examples l31 are included to demonstrate operable inhibitor compositions and to illustrate the necessity of observing the limitations above set forth. Each of the compositions set forth was applied to a cylindrical grain of double-base smokeless powder containing nitroglycerin by concentrically disposing the powder grain in an oversized cylindrical mold equipped with a steam jacket and filling the resulting annulus between grain and mold with the uncured mix. The composition was cured for about one hour at a temperature of C. After removal from the mold, the restriction and bond were examined. The inhibited grains were then placed in hot storage and unless otherwise indicated, were maintained at about 60 C. for a period of three weeks and examined at weekly intervals. forth in-Table -1 under Remarks. 'All the compositions in Table 1 contained about 4% of Luperco ATC (a 50:50 mixture of benzoyl peroxide and tricresyl phos phate) as a polymerization catalyst.
TABLE 1 Plasticizer Percent Cross- Remarks linking Agent good bond-good plastic. bond failed in hot storage-plastic softened. good bondgood plastic. satisfactory bondplastic satisfactory but soigencd somewhat after hot storage.
good bond-good plastic. good bondgood plasticuncured mix thin with slight settling out of PMMA. bontlijfailed in hot storageplastic softened. 0.
good bond-plastic satisfactory but somewhat brittle. bond failed inhot storage-plastic cracked.
The'observations made are set i TABLE, IQ-Co'ntinued BMA PMMA Plastieizer Percent Crossg Agent Remarks 25 (15% DAP) 15(10% TCP).
b) M03 one. 8
co can cc c5 so 7 9 to woo woo o co o o M HM m an O0 8o 8 88 8 C we: co c: we:
In Table 2, Examples 32-37 are presented to illustrate the criticality of the 95/5 ratio of PVC/PVA. Thirty (30) percent of the PVC-PVA copolymer was employed 5 DVB (18%)--- 10 DVB (18%) 1o DVB 45% 5 DvB 45% 10 BCM in 2111 cases. 1 The commercial designation of the polymer 40 employed is set forth in parenthesis. The inhibitor was applied to double-base smokeless powder grains by the bond good (in hot storage the plastic softened undesirably). good bond-good plastic. satisfactory bondplastic satisfactory but softened somewhat in hot storage. good bond-plastic satisfactory but exhibited slight softening in hot storage. bond failed in hot storageplastic softened. satisfactory bond-plastic satisfactory but softened slightly. 1 bond failed in hot storage-plastic satisfactory. satisfactory bond-plastic satisfactory but becoming brittleuncured mix thin and some PMMA settled out while standing. bond failed in hot storageplastic satisfactory -uncured mix was very thin allowing the PMMA to settle out. good bond-good plastic.
satisfactory bondsatisfactory plasticuncured mix viscous and difiicult to handle. satisfactory bond-plastic satisfactory but showed some softening in storage. satisfactory bond-satisfactory plastic-uncured mix viscous and difficult to handle. bond failedplastic very brittle and cracked. good bondgood plastic-excellent temperature properties. good initial bond-good plastic-bond failed after extended storage at 66 0. good initial bond-plastic satisfactory although somewhat brittle. good bondgood plastic. good initial bond-good plastic-bond failed after extended storage at 66 0. good bond-good plasticexcellent temperature properties.
outer surfaces of the remaining groups were restricted in accordance with the invention. The outer surfaces of group 2 were restricted by casting around the grains a mix containing 40% monomeric butyl methacrylate,
polyvinyl chloride-acetate copolymer, 20% polymethyl methacrylate, and 10% of tricresyl phosphate. Two percasting process employed in Examples 1-31. Observacent of benzoyl peroxide based on the weight of butyl tions are given under Remarks. methacrylate monomer was employed as polymerization TABLE 2 Exlaimple BMA PMMA PL PVC/PVA Catalyst* Remarks 32 40 20 10 TOP.-- 95/5 (VYNV-l) p 4 excellent for all uses except extended hot storage. 33 40 20 10 TGP 8588/12-15 (VYHH) 4 very thick, very tacky, air
bubblesno casting. 34 40 2O 10 TOP-.- 100/-(QYNV) 4 Bond failed-becomes very g softinhot storage. 35 4o 20 10 TOP.-- ss.5-91.5/s.5-11.5 4 very thick-air bubbles-no (VYNS-3) casting. 1 36. 20' 10 TCP 100/ (Geon 121) 4 bond failure. 37 40 20 10 SEER... 100l-(Geon 121) 4 Do.
7 BMiX-n -butyl methacrylate monomer. PMMA-polymethyl methacrylate. F66 r iiii i 1 111 d t t 1 -p0 yvmy c on e ace a e copo ymer. TCP-tricresyl phosphate. SHP-di-Z-ethylhexyl tetrahydrophthalate.
Catalyst-Luperco ATO (/50 benzoyl peroxide) tricrcsyl phosphate.
"Even when the-amount of PVA in the copolymer is 5% or less, difiiculty is sometimes encountered in obtaining a casting if the particle size of the copolymer is unduly large The copolymers which are commercially produced for plastisols and organosols and contain less than 5% of PVA are generally satisfactory as furnished. Any difi'iculty encountered can be overcome by allowing -more time for the copolymer to go into solution or by ball-milling the PVC-A to reduce particle size before .use.
Example 38 Four groups of solid, cylindrical, end-burning grains were prepared. The outer surfaces of group 1 were con- 60 C. storage for 36 weeks and at the end of each week a grain from each group was removed and its restriction analyzed to determine nitroglycerin absorption. In the analysis the standard TiCl method on a methylene chloride extract was employed. At the end of 12 weeks the cellulose acetate restriction contained 29% by weight ventionally restricted with cellulose acetate, while the of nitroglycerin. At the end of 12 weeks it was noted that nitroglycerin absorption had practically leveled off in all the restrictions. At the end of 36 weeks, the restrictions of groups 2, 3, and 4 contained a maximum of 8%, and 7.5%, respectively.
Example 39 Restricted grains similar to those of groups 2, 3, and 4 were placed in 80 C. storage for 9 weeks. Bond failures occured in group 2 at the end of two days. At the end of 9 weeks plastic and bonds in groups 3 and 4 were oxide is especially preferred in view of the low temperature necessary to effect polymerization with this material.
. In some applications it may be desired to incorporate a filler material in the restriction composition such as glass wool, asbestos fioc, and the like.
Since modifications of the invention will be apparent to the art, the invention is limited only by the scope of excellent. Maximum absorption of nitroglycerin in group I 3 was 10.7% and in group 4 was 9.8%.
The plastic inhibitor compositions of the invention may be applied to external or perforation surfaces of gasproducing charges in any desired manner. The preferred method is to place an unrestricted grain into an oversized mold and then introduce the curable mix or slurry into the annulus around the grain in such a manner as to prevent entrapment of air. This is best accomplished by introducing the mix under pressure into the base of the mold. The entire mold is then subjected to curing conditions until the plastic has set and a bond has been formed. Perforation surfaces may be similarly inhibited by employing undersized forms and then introducing the uncured mix into the space between form and perforation surface. Alternatively, the plastic inhibitor may be initially molded and the propellant grain subsequently cast in the hollow inhibitor cylinder, thus using this cylinder as a mold or casting container. A satisfactory bond is obtained between inhibitor and grain during the curing of the grain. In other instances it may be desired to apply the composition by crosshead extrusion techniques. Another operable method, although not as desirable, is to separately prefabricate both the inhibitor and the grain to close tolerances, apply a mutual solvent to the surface of the grain, and then slide the grain into the inhibitor cylinder.
It is especially preferred, however, to cast the inhibitor around the finished grain or in a perforation, since it is by this procedure that the best bond is obtained. The enhanced bond thus produced results from the solvent action of the monomeric butyl methacrylate monomer on the nitrocellulose on the surface of the gas-producing grain. Since the butyl methacrylate is also a solvent for the polymeric constituents of the inhibitor, the nitrocellulose polymer and the polyvinyl chloride acetatepolymethyl methacrylate of the inhibitor are held in mutual solution at the surface of the grain. Thus, when the butyl methacrylate is polymerized, a strong bond is obtained. The strength of this bond and the ruggedness of the inhibitor composition as a whole is further enhanced by cross-linking of the butyl methacrylate when the bifunctional cross-linking monomer such as BCM or divinylbenzene is employed.
It has been found that any of the conventional plasticizers for PVC-A employed by the art are operable when employed in the critical amount. Of all of those employed, however, tricresyl phosphate is preferred in view of its plasticizing properties and further in view of its fireproofing effect on the composition. Other plasticizers which may be employed include, without limitation, diallyl phthalate, trioctyl phthalate, trioctyl phosphate, dibutyl sebacate, and dibutyl adipate.
A variety of polymerization catalysts for acrylic monomers are known to the art and may be employed in place of any of the catalysts illustrated by the examples. Such materials include lauroyl peroxide, di-tert-butyl peroxide, tertiary butyl hydroperoxide, cumene hydroperoxide, methyl ethyl ketone peroxide, and tertiary butyl perbenzoate. Of all of the operable catalysts those of the peroxide type are the most desirable. Benzoyl perthe appended claims.
What we claim and desire to protect by Letters Patent V 1. A curable mixture adapted for inhibitor application to combustible gas-producing charges comprising by weight from 25 to 50% monomeric butyl methacrylate, from 25 to 45% of a copolymer of vinyl chloride with not more than about 5% of vinyl acetate, from 5 to 30% of polymeric methyl methacrylate, and from 5 to 20% of a nonvolatile plasticizer for the vinyl chloride-vinyl acetate copolymer.
, 2. A mixture according to claim 1 containing a polymerization catalyst for monomeric butyl methacrylate.
3. A mixture according to claim 1 in which the plasticizer is tricresyl phosphate. 4. A curable mixture adapted for inhibitor application to combustible gas-producing charges comprising by weight from 25to 50% monomeric butyl methacrylate, from 25 to 45 of a copolymer of vinyl chloride with not more than about 5% of vinyl acetate, from 5 t6 30% of polymeric methyl methacrylate, an amount not exceeding 15% of the dimethacrylate of ethylene glycol,
and from 5 to 20% of a nonvolatile plasticizer for the vinyl chloride-vinyl acetate copolymer.
5. A mixture according to claim 4 containing a polymerization catalyst for monomeric butyl methacrylate.
6. A mixture according to claim 4 in whichthe'p'lasticizer is tricresyl phosphate.
7. A composition of matter comprising the cured product of a mixture containing from 25 to 50% monomeric butyl methacrylate, from 25 to 45 of a copolymer of vinyl chloride with not more than about 5% of vinyl acetate, from 5 to 30% of polymeric methyl methacrylate, and from 5 to 20% of a nonvolatile plasticizer for-the vinyl chloride-vinyl acetate copolymer, said product being adapted for inhibitor application to a combustible gasproducing charge.
8. A composition according to claim 7 in which the plasticizer is tricresyl phosphate.
9. A composition of matter comprising the cured product of a mixture containing from 25 to 50% monom'er ic butyl methacrylate, from 25 to 45 of a copolymer of vinyl chloride with not more than about 5% of vinyl acetate, from 5 to 30% of polymeric methyl methacrylate, an amount not exceeding 15 of the dimethacrylate of ethylene glycol, and from 5 to 20% of a nonvolatile plasticizer for the vinyl chloride-vinyl acetate copolymer, said product being adapted for inhibitor application to a combustible gas-producing charge.
10. A composition according to claim 9 in which the plasticizer is tricresyl phosphate.
References Cited in the file of this patent UNITED STATES PATENTS 2,155,591 Garvey Apr. 25, 1939 2,392,857 McGill Jan. 15, 1946 2,476,993 Milton et al July 26, 1949 2,498,388 Ball Feb. 21, 1950 2,643,184 Cairns June 23,1953 2,657,191 Coover et a1. Oct. 27, 1953 2,666,042 Nozaki "Jan. 12, 1954 FOREIGN PATENTS 540,383 Great Britain Oct. 15, 1941
Claims (1)
1. A CURABLE MIXTURE ADAPTED FOR INHIBITOR APPLICATION TO COMBUSTIBLE GAS-PRODUCING CHARGES COMPRISING BY WEIGHT FROM 25 TO 50% MONOMERIC BUTYL METHACRYLATE, FROM 25 TO 45% OF A COPOLYMER OF VINYL CHLORIDE WITH NOT MORE THAN ABOUT 5% OF VINYL ACATATE, FROM 5 TO 30% OF POLYMERIC METHYL METHACRYLATE, AND FROM 5 TO 20% OF A NONVOLATILE PLASTICIZER FOR THE VINYL CHLORIDE-VINYL ACETATE COPOLYMER.
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US357384A US2858289A (en) | 1953-05-25 | 1953-05-25 | Combustion inhibitor for gas-producing charges |
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US357384A US2858289A (en) | 1953-05-25 | 1953-05-25 | Combustion inhibitor for gas-producing charges |
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Cited By (15)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
US2989388A (en) * | 1958-03-17 | 1961-06-20 | Ohio Commw Eng Co | Fuel and propellant composition |
US3036977A (en) * | 1957-08-17 | 1962-05-29 | Hoechst Ag | Aqueous dispersions of adhesive vinyl polymeric materials containing carboxylic acid ester additives |
US3046829A (en) * | 1959-06-22 | 1962-07-31 | Olin Mathieson | Composite propellent grains |
US3048076A (en) * | 1962-08-07 | Method of inhibiting propellent | ||
US3060687A (en) * | 1957-10-31 | 1962-10-30 | Standard Oil Co | Temperature rise retardation of surface exposed to heat |
US3069845A (en) * | 1958-03-14 | 1962-12-25 | Mini Of Supply | Liner for cooling rocket motors |
US3107573A (en) * | 1960-10-28 | 1963-10-22 | Standard Oil Co | Method of restricting a solid propellant |
DE1161506B (en) * | 1960-06-24 | 1964-01-16 | Atlantic Res Corp | Solid propellant mass |
US3250829A (en) * | 1963-03-03 | 1966-05-10 | Thiokol Chemical Corp | Method of making a combustioninhibited solid propellant grain |
US3306790A (en) * | 1967-02-28 | Slow burning plastisol cellulose ace- tate propellant composition contain- ing resorcinol | ||
US4106960A (en) * | 1976-02-03 | 1978-08-15 | Dynamit Nobel Aktiengesellschaft | Temperature-compensating propellant charge |
US4185557A (en) * | 1972-04-28 | 1980-01-29 | The United States Of America As Represented By The Secretary Of The Navy | Stress reducing liner and method of fabrication |
US4445948A (en) * | 1980-06-02 | 1984-05-01 | The United States Of America As Represented By The Secretary Of The Navy | Polymer modified TNT containing explosives |
US4453860A (en) * | 1977-03-02 | 1984-06-12 | Dynamit Nobel Aktiengesellschaft | Firedamp-safe method for stud driving cartridges |
US6026749A (en) * | 1973-05-11 | 2000-02-22 | Imperial Metal Industries (Kynoch) Limited | Multiple base propellant with combustion inhibitor |
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US2643184A (en) * | 1944-01-15 | 1953-06-23 | Us Sec War | Propellent charge for jet-propelled devices |
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GB540383A (en) * | 1939-08-08 | 1941-10-15 | Bakelite Ltd | Improvements in or relating to moulding compositions |
US2392857A (en) * | 1942-04-10 | 1946-01-15 | Ici Ltd | Sheet materials comprising polyvinyl chloride |
US2643184A (en) * | 1944-01-15 | 1953-06-23 | Us Sec War | Propellent charge for jet-propelled devices |
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US2476993A (en) * | 1948-02-02 | 1949-07-26 | Jr Clare L Milton | Process for making molds |
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Cited By (15)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
US3306790A (en) * | 1967-02-28 | Slow burning plastisol cellulose ace- tate propellant composition contain- ing resorcinol | ||
US3048076A (en) * | 1962-08-07 | Method of inhibiting propellent | ||
US3036977A (en) * | 1957-08-17 | 1962-05-29 | Hoechst Ag | Aqueous dispersions of adhesive vinyl polymeric materials containing carboxylic acid ester additives |
US3060687A (en) * | 1957-10-31 | 1962-10-30 | Standard Oil Co | Temperature rise retardation of surface exposed to heat |
US3069845A (en) * | 1958-03-14 | 1962-12-25 | Mini Of Supply | Liner for cooling rocket motors |
US2989388A (en) * | 1958-03-17 | 1961-06-20 | Ohio Commw Eng Co | Fuel and propellant composition |
US3046829A (en) * | 1959-06-22 | 1962-07-31 | Olin Mathieson | Composite propellent grains |
DE1161506B (en) * | 1960-06-24 | 1964-01-16 | Atlantic Res Corp | Solid propellant mass |
US3107573A (en) * | 1960-10-28 | 1963-10-22 | Standard Oil Co | Method of restricting a solid propellant |
US3250829A (en) * | 1963-03-03 | 1966-05-10 | Thiokol Chemical Corp | Method of making a combustioninhibited solid propellant grain |
US4185557A (en) * | 1972-04-28 | 1980-01-29 | The United States Of America As Represented By The Secretary Of The Navy | Stress reducing liner and method of fabrication |
US6026749A (en) * | 1973-05-11 | 2000-02-22 | Imperial Metal Industries (Kynoch) Limited | Multiple base propellant with combustion inhibitor |
US4106960A (en) * | 1976-02-03 | 1978-08-15 | Dynamit Nobel Aktiengesellschaft | Temperature-compensating propellant charge |
US4453860A (en) * | 1977-03-02 | 1984-06-12 | Dynamit Nobel Aktiengesellschaft | Firedamp-safe method for stud driving cartridges |
US4445948A (en) * | 1980-06-02 | 1984-05-01 | The United States Of America As Represented By The Secretary Of The Navy | Polymer modified TNT containing explosives |
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