US3539377A - Method for coating oxidizer particles with a polymer - Google Patents

Method for coating oxidizer particles with a polymer Download PDF

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Publication number
US3539377A
US3539377A US727340A US3539377DA US3539377A US 3539377 A US3539377 A US 3539377A US 727340 A US727340 A US 727340A US 3539377D A US3539377D A US 3539377DA US 3539377 A US3539377 A US 3539377A
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polymer
solvent
coating
oxidizer
particles
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US727340A
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Melvin E Steinle
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US Department of Army
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US Department of Army
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    • BPERFORMING OPERATIONS; TRANSPORTING
    • B01PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
    • B01JCHEMICAL OR PHYSICAL PROCESSES, e.g. CATALYSIS OR COLLOID CHEMISTRY; THEIR RELEVANT APPARATUS
    • B01J2/00Processes or devices for granulating materials, e.g. fertilisers in general; Rendering particulate materials free flowing in general, e.g. making them hydrophobic
    • B01J2/006Coating of the granules without description of the process or the device by which the granules are obtained

Definitions

  • This invention relates to an improved process for coating compound particles and more specifically to an improved process for coating a solid oxidizer with a polymer utilizing a solvent-non-solvent technique.
  • the interfacial reactions at and within the surface release sufiicient heat to expel partially combusted products, pyrolysis products, and fuel and oxidizer fragments into the gas zone above the surface where they intermix and burn completely.
  • the maximum flame temperature is reached in the luminous zone where the largest portion of heat is released.
  • only a small amount of heat released in the luminous flame zone reaches the surface to supplement the heat generated by the interfacial reactions.
  • One method for controlling the contributions of interfacial reactions in the combustion process is to change the reactivity of the interface by coating the oxidizer particles. Because coating materials are available for both increasing and decreasing this reactivity, this approach represents a convenient method for varying the interfacial reactivity over a relatively wide range.
  • the present invention relates to an improved process for coating an oxidizer with a polymer utilizing a solventnon-solvent technique.
  • the coating polymer ice A sufficient quantity of non-solvent is added to harden the polymer.
  • the liquid phase is removed by decantation and the coated material removed.
  • ethyl cellulose is first dissolved in 300 grams of methylene chloride.
  • the OH groups in the cellulose utilized have been partly or completely replaced by ethoxyl groups.
  • the solution and 394 grams of ammonium perchlorate having a particle size of about microns are added to a mixer bowl and agitated on a modified Hobart mixer at ambient temperature. During agitation, a nitrogen flush is utilized to draw olf the excess methylene chloride.
  • methylene chloride has been substantially removed and the mixture has the appearance of a thick gel, an initial portion of a. total of 1000 ml.
  • Freon (1,1,2-trichloro-l,2,2-trifluoro ethane) is added slowly with agitation to bring the ethyl cellulose out of solution and to coat the ammonium perchlorate.
  • a hardening agent e.g. 0.06 gram of tetrabutyl titanate
  • the agitation is stopped and the liquid phase removed.
  • a second portion of Freon is added and the coated ammonium perchlorate agitated for a period of ten minutes. Subsequently, the liquid phase is removed and the recovered wet polymer coated ammonium perchlorate dried.
  • the polymer coated onto an ammonium perchlorate particle by this method does not react with the ammonium perchlorate and therefore cannot alter the oxidizer in any chemical manner.
  • the removed solvent is immediately ready for reuse in the next batch.
  • the polymer in the gel state will precipitate out in the non-solvent much faster with most of the solvent removed.
  • a much larger quantity of material can be coated in a smaller volume container in that when the non-solvent is added, most of the solvent has been removed.
  • Kel-F-800 polychlorotrifiuoroethylene
  • Hypalon chorosulfonated polyethylene
  • Kel-F-800 polychlorotrifiuoroethylene
  • Hypalon chorosulfonated polyethylene
  • Any solvent-non-solvent system is operable provided the polymer utilized is soluble in one and insoluble in the other, respectively.
  • a process for coating solid particles of an oxidizer with a polymer selected from the group consisting of ethyl cellulose, polychlorotrifluoroethylene and chlorosulfonated polyethylene comprising the steps of: dissolving the polymer in a solvent which is a nonsolvent in relation to the oxidizer, adding the oxidizer to the resultant solution, agitating and substantially removing all of the solvent until the mixture has the appearance of a gel, adding a liquid which is a nonsolvent in relation to the polymer along with a polymer hardening agent, agitating, and recovering the coated oxidizer.

Description

United States Patent O US. Cl. 11762.2 7 Claims ABSTRACT OF THE DISCLOSURE A process for coating compound particles with a polymer comprising, dissolving the polymer in a solvent, adding the particles to the resultant solution and agitating while drawing off the solvent. On the substantial removal of the solvent, a non-solvent is added, and the coated particles recovered.
This invention relates to an improved process for coating compound particles and more specifically to an improved process for coating a solid oxidizer with a polymer utilizing a solvent-non-solvent technique.
Unstable combustion of solid propellants has at times presented serious problems in the development of operational solid propellant propulsion systems. Studies on the structure of a combustion zone has presented evidence that there are significant exothermic processes which occur on and within the solid phase propellant. The results of these studies indicate the combustion process is controlled by two interdependent exothermic reaction zones near and on the surface of the propellant. One zone is in the gas phase at a finite distance away from the solid propellant surface and is characterized by interdillusion of gasified oxidizer and fuel species and combustion of particles of ejected matter from the surface. The secondary reaction zone occurs on and within the solid propellant surface. The primary release in this zone probably occurs from chemical reactions between the initial decomposition products of a solid oxidizer and an adjacent fuel surface.
The interfacial reactions at and within the surface release sufiicient heat to expel partially combusted products, pyrolysis products, and fuel and oxidizer fragments into the gas zone above the surface where they intermix and burn completely. The maximum flame temperature is reached in the luminous zone where the largest portion of heat is released. However, because of the relatively large mass flow perpendicular to the surface, only a small amount of heat released in the luminous flame zone reaches the surface to supplement the heat generated by the interfacial reactions.
One method for controlling the contributions of interfacial reactions in the combustion process is to change the reactivity of the interface by coating the oxidizer particles. Because coating materials are available for both increasing and decreasing this reactivity, this approach represents a convenient method for varying the interfacial reactivity over a relatively wide range.
The present invention relates to an improved process for coating an oxidizer with a polymer utilizing a solventnon-solvent technique. In the process, the coating polymer ice A sufficient quantity of non-solvent is added to harden the polymer. The liquid phase is removed by decantation and the coated material removed.
It is an object of this invention to provide and disclose an improved process for coating particles of a compound with a polymer.
It is a further object of this invention to provide and disclose an improved process for coating an oxidizer, utilized in a solid propellant system, with a polymer.
Other objects and a fuller understanding of the invention may be ascertained from the following description and claims.
In the process, 6 grams of ethyl cellulose is first dissolved in 300 grams of methylene chloride. The OH groups in the cellulose utilized have been partly or completely replaced by ethoxyl groups. The solution and 394 grams of ammonium perchlorate having a particle size of about microns are added to a mixer bowl and agitated on a modified Hobart mixer at ambient temperature. During agitation, a nitrogen flush is utilized to draw olf the excess methylene chloride. When methylene chloride has been substantially removed and the mixture has the appearance of a thick gel, an initial portion of a. total of 1000 ml. of Freon (1,1,2-trichloro-l,2,2-trifluoro ethane) is added slowly with agitation to bring the ethyl cellulose out of solution and to coat the ammonium perchlorate. At this point, a small amount of a hardening agent, e.g., 0.06 gram of tetrabutyl titanate, may be added. After the mixture is agitated for a period of fifteen minutes, the agitation is stopped and the liquid phase removed. A second portion of Freon is added and the coated ammonium perchlorate agitated for a period of ten minutes. Subsequently, the liquid phase is removed and the recovered wet polymer coated ammonium perchlorate dried.
The polymer coated onto an ammonium perchlorate particle by this method does not react with the ammonium perchlorate and therefore cannot alter the oxidizer in any chemical manner. By removing most of the solvent prior to adding a non-solvent, the removed solvent is immediately ready for reuse in the next batch. Furthermore, the polymer in the gel state will precipitate out in the non-solvent much faster with most of the solvent removed. In addition, a much larger quantity of material can be coated in a smaller volume container in that when the non-solvent is added, most of the solvent has been removed.
In addition to ethyl cellulose, other polymers, e.g., Kel-F-800 (polychlorotrifiuoroethylene) and Hypalon (chorosulfonated polyethylene) may be utilized to coat the ammonium perchlorate. When Kel-F-800 is used, e.g., Freon is utilized as the solvent and methylene chloride as the non-solvent. Any solvent-non-solvent system is operable provided the polymer utilized is soluble in one and insoluble in the other, respectively.
Although I have described my invention with a certain degree of particularity, it is understood that the foregoing is made to set forth the best mode contemplated in carrying out the invention and not as a limitation thereof, in that many substitutions may be made, for example, in the utilization of polymers, particles of compounds to be coated, solvents and non-solvents, without the vitiation of the operability of the invention.
Having described my invention, I claim:
1. A process for coating solid particles of an oxidizer with a polymer selected from the group consisting of ethyl cellulose, polychlorotrifluoroethylene and chlorosulfonated polyethylene comprising the steps of: dissolving the polymer in a solvent which is a nonsolvent in relation to the oxidizer, adding the oxidizer to the resultant solution, agitating and substantially removing all of the solvent until the mixture has the appearance of a gel, adding a liquid which is a nonsolvent in relation to the polymer along with a polymer hardening agent, agitating, and recovering the coated oxidizer.
2. A process in accordance with claim 1 wherein the oxidizer is ammonium perchlorate.
3. A process in accordance with claim 2 wherein the polymer is ethyl cellulose.
4. A process in accordance with claim 3 wherein the hardening agent is tetrabutyl titanate.
5. A process in accordance with claim 4 wherein the solvent is methylene chloride and the non-solvent 1,1,2- trichloro-1,2,2-trifluoroethane.
6. A process in accordance with claim 2 wherein the polymer is polychlorotrifluoroethylene.
7. A process in accordance with claim 6 wherein the solvent is 1,1,2-trichloro-1,2,2 -trifluoroethane and the non-solvent is methylene chloride.
References Cited UNITED STATES PATENTS Waldeck 117-166 X Hetherington et a1. 117161 X Carstensen et a1. 117109 X Butler et al. 149-76 X Hiestand et al 117100 X Rowe 117100 Vassiliades 117--100 X Vassiliades 117100 Woods et al. 1497 WILLIAM D. MARTIN, Primary Examiner 15 M. R. P. PERRONE, .TR., Assistant Examiner US. Cl. X.R.
US727340A 1968-05-07 1968-05-07 Method for coating oxidizer particles with a polymer Expired - Lifetime US3539377A (en)

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Cited By (12)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
US3650858A (en) * 1970-02-24 1972-03-21 Us Air Force Surface treatment process for solid rocket propellant composition
US3659785A (en) * 1970-12-08 1972-05-02 Us Air Force Weather modification utilizing microencapsulated material
US3776787A (en) * 1971-11-23 1973-12-04 Ici Ltd Granular propellant containing kno{11 {11 and unsaturated ester
US3891482A (en) * 1970-04-27 1975-06-24 Us Army Propellant instability modifier
US3935339A (en) * 1973-07-16 1976-01-27 Exxon Production Research Company Method for coating particulate material thereof
US3953257A (en) * 1973-09-07 1976-04-27 The United States Of America As Represented By The Secretary Of The Army Method for preparing small particle size coated ammonium perchlorate
US3954526A (en) * 1971-02-22 1976-05-04 Thiokol Corporation Method for making coated ultra-fine ammonium perchlorate particles and product produced thereby
US3976521A (en) * 1974-11-20 1976-08-24 The United States Of America As Represented By The Secretary Of The Air Force Method of coating boron particles with ammonium perchlorate
US4367103A (en) * 1979-03-07 1983-01-04 Imperial Chemical Industries Limited Explosive composition
US4389264A (en) * 1980-02-21 1983-06-21 S.A. Prb, Societe Anonyme Process for the manufacture of insulated propellant sets and of propelling sets provided with an insulating envelope
US4452145A (en) * 1980-02-21 1984-06-05 S.A. Prb Societe Anonyme Propellant for base-bleed gas generators and process for manufacturing it
US4698106A (en) * 1971-12-16 1987-10-06 The United States Of America As Represented By The Secretary Of The Army Method for the manufacture of oxidizers of very large surface area and their use in high burning rate propellants

Citations (9)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
US2111342A (en) * 1936-10-02 1938-03-15 Pittsburgh Plate Glass Co Caustic resistant material
US2782174A (en) * 1952-10-08 1957-02-19 Kellogg M W Co Dispersions of perfluorocarbon polymers
US2789920A (en) * 1955-12-19 1957-04-23 American Cyanamid Co Method of coating gelatin capsules with ethyl cellulose
US3052577A (en) * 1958-04-09 1962-09-04 Olin Mathieson Smoke forming compositions
US3242051A (en) * 1958-12-22 1966-03-22 Ncr Co Coating by phase separation
US3336155A (en) * 1964-01-15 1967-08-15 Ncr Co Process of coating particles with a polymer
US3418250A (en) * 1965-10-23 1968-12-24 Us Plywood Champ Papers Inc Microcapsules, process for their formation and transfer sheet record material coated therewith
US3418656A (en) * 1965-10-23 1968-12-24 Us Plywood Champ Papers Inc Microcapsules, process for their formation and transfer sheet record material coated therewith
US3441455A (en) * 1961-01-13 1969-04-29 Continental Oil Co Encapsulated propellants and method for their preparation from fluorinated monomers using radiation

Patent Citations (9)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
US2111342A (en) * 1936-10-02 1938-03-15 Pittsburgh Plate Glass Co Caustic resistant material
US2782174A (en) * 1952-10-08 1957-02-19 Kellogg M W Co Dispersions of perfluorocarbon polymers
US2789920A (en) * 1955-12-19 1957-04-23 American Cyanamid Co Method of coating gelatin capsules with ethyl cellulose
US3052577A (en) * 1958-04-09 1962-09-04 Olin Mathieson Smoke forming compositions
US3242051A (en) * 1958-12-22 1966-03-22 Ncr Co Coating by phase separation
US3441455A (en) * 1961-01-13 1969-04-29 Continental Oil Co Encapsulated propellants and method for their preparation from fluorinated monomers using radiation
US3336155A (en) * 1964-01-15 1967-08-15 Ncr Co Process of coating particles with a polymer
US3418250A (en) * 1965-10-23 1968-12-24 Us Plywood Champ Papers Inc Microcapsules, process for their formation and transfer sheet record material coated therewith
US3418656A (en) * 1965-10-23 1968-12-24 Us Plywood Champ Papers Inc Microcapsules, process for their formation and transfer sheet record material coated therewith

Cited By (12)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
US3650858A (en) * 1970-02-24 1972-03-21 Us Air Force Surface treatment process for solid rocket propellant composition
US3891482A (en) * 1970-04-27 1975-06-24 Us Army Propellant instability modifier
US3659785A (en) * 1970-12-08 1972-05-02 Us Air Force Weather modification utilizing microencapsulated material
US3954526A (en) * 1971-02-22 1976-05-04 Thiokol Corporation Method for making coated ultra-fine ammonium perchlorate particles and product produced thereby
US3776787A (en) * 1971-11-23 1973-12-04 Ici Ltd Granular propellant containing kno{11 {11 and unsaturated ester
US4698106A (en) * 1971-12-16 1987-10-06 The United States Of America As Represented By The Secretary Of The Army Method for the manufacture of oxidizers of very large surface area and their use in high burning rate propellants
US3935339A (en) * 1973-07-16 1976-01-27 Exxon Production Research Company Method for coating particulate material thereof
US3953257A (en) * 1973-09-07 1976-04-27 The United States Of America As Represented By The Secretary Of The Army Method for preparing small particle size coated ammonium perchlorate
US3976521A (en) * 1974-11-20 1976-08-24 The United States Of America As Represented By The Secretary Of The Air Force Method of coating boron particles with ammonium perchlorate
US4367103A (en) * 1979-03-07 1983-01-04 Imperial Chemical Industries Limited Explosive composition
US4389264A (en) * 1980-02-21 1983-06-21 S.A. Prb, Societe Anonyme Process for the manufacture of insulated propellant sets and of propelling sets provided with an insulating envelope
US4452145A (en) * 1980-02-21 1984-06-05 S.A. Prb Societe Anonyme Propellant for base-bleed gas generators and process for manufacturing it

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