U.S. patent application number 10/913182 was filed with the patent office on 2005-05-05 for low-sensitivity explosive compositions and method for making explosive compositions.
Invention is credited to Braithwaite, Paul C., Lee, Kenneth E., Mezger, Mark, Nicolich, Steve.
Application Number | 20050092407 10/913182 |
Document ID | / |
Family ID | 23198019 |
Filed Date | 2005-05-05 |
United States Patent
Application |
20050092407 |
Kind Code |
A1 |
Lee, Kenneth E. ; et
al. |
May 5, 2005 |
Low-sensitivity explosive compositions and method for making
explosive compositions
Abstract
An explosive composition is provided that includes 85 to about
96 weight percent nitramine, based on the total composition weight,
and about 4 to 15 weight percent plasticized binder. At least 80
weight percent of the total composition weight, and more preferably
85 to 96 weight percent of the total composition weight, comprises
2,4,6,8,10,12-hexanitro-2,4,6,8,1-
0,12-hexaazatetracyclo[5.5.0.0.sup.5,90.sup.3,11]-dodecane (CL-20)
particles having an average particle size not greater than 30
microns as the nitramine. Methods for preparing an explosive from
the explosive composition are also provided.
Inventors: |
Lee, Kenneth E.; (North
Ogden, UT) ; Braithwaite, Paul C.; (Brigham City,
UT) ; Nicolich, Steve; (Wyckoff, NJ) ; Mezger,
Mark; (Mount Bethel, PA) |
Correspondence
Address: |
TRASK BRITT
P.O. BOX 2550
SALT LAKE CITY
UT
84110
US
|
Family ID: |
23198019 |
Appl. No.: |
10/913182 |
Filed: |
August 5, 2004 |
Related U.S. Patent Documents
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Application
Number |
Filing Date |
Patent Number |
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10913182 |
Aug 5, 2004 |
|
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|
10210863 |
Jul 31, 2002 |
|
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60309386 |
Aug 1, 2001 |
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Current U.S.
Class: |
149/109.6 |
Current CPC
Class: |
C06B 25/34 20130101;
C06B 21/0083 20130101; C06B 45/105 20130101; C06B 45/24
20130101 |
Class at
Publication: |
149/109.6 |
International
Class: |
D03D 023/00 |
Goverment Interests
[0002] The U.S. Government has a paid-up license in this invention
and the right in limited circumstances to require the patent owner
to license others on reasonable terms as provided for by the terms
of DAAE30-98-D-1005 awarded by the Picatinny Arsenal of the U.S.
Army.
Claims
What is claimed is:
1. A method for preparing an explosive, comprising: combining
2,4,6,8,10,12-hexanitro-2,4,6,8,10,12-hexaazatetracyclo[5.5.0.0.sup.5,90.-
sup.3,11]-dodecane (CL-20) particles having an average particle
size not greater than 30 microns with a plasticized binder to form
an explosive composition; and granulating the explosive composition
into the explosive, the explosive comprising 85 weight percent to
about 96 weight percent of the CL-20 particles and about 4 weight
percent to 15 weight percent of the plasticized binder.
2. The method of claim 1, wherein combining CL-20 particles having
an average particle size not greater than 30 microns with the
plasticized binder comprises combining CL-20 particles having an
average particle size of not greater than 10 microns with the
plasticized binder.
3. The method of claim 1, wherein combining CL-20 particles having
an average particle size not greater than 30 microns with the
plasticized binder comprises combining CL-20 particles having an
average particle size in a range of 1 micron to 4 microns with the
plasticized binder.
4. The method of claim 1, wherein combining CL-20 particles having
an average particle size not greater than 30 microns with the
plasticized binder comprises combining CL-20 particles having an
average particle size in a range of 1 micron to 2 microns with the
plasticized binder.
5. The method of claim 1, wherein combining CL-20 particles having
an average particle size not greater than 30 microns with the
plasticized binder to form the explosive composition comprises
forming the explosive composition to have 100 percent of the CL-20
particles having a particle size less than 10 microns.
6. The method of claim 1, wherein combining CL-20 particles having
an average particle size not greater than 30 microns with the
plasticized binder to form the explosive composition comprises
forming the explosive composition to have 100 percent of the CL-20
particles having a particle size less than 4 microns.
7. The method of claim 1, wherein combining CL-20 particles having
an average particle size not greater than 30 microns with the
plasticized binder to form the explosive composition comprises
forming the explosive composition to have the CL-20 particles at 85
weight percent to 95 weight percent of a total weight of the
explosive composition.
8. The method of claim 1, wherein combining CL-20 particles having
an average particle size not greater than 30 microns with the
plasticized binder to form the explosive composition comprises
forming the explosive composition to have the CL-20 particles at 94
weight percent to 95 weight percent of a total weight of the
explosive composition.
9. The method of claim 1, wherein combining CL-20 particles having
an average particle size not greater than 30 microns with the
plasticized binder comprises combining the CL-20 particles with
cellulose acetate butyrate and bis-dinitropropyl
acetal/bis-dinitropropyl formal.
10. The method of claim 1, wherein the explosive composition has a
shock sensitivity under 140 cards, as measured by the NOL Card Gap
Test.
11. A method for preparing an explosive having a total weight, the
method comprising: providing an aqueous dispersion comprising
epsilon polymorph CL-20 particles, the CL-20 particles having an
average particle size not greater than 30 microns; combining the
aqueous dispersion with a lacquer comprising a plasticized binder
to form a slurry; agitating the slurry and removing the lacquer to
form coated granules; and drying the coated granules to provide an
explosive having a total weight, the total weight of the dry coated
granules comprising 85 weight percent to about 96 weight percent
CL-20 and about 4 weight percent to 15 weight percent of the
plasticized binder.
12. The method of claim 11, wherein providing the aqueous
dispersion comprising epsilon polymorph CL-20 particles comprises
providing the aqueous dispersion comprising epsilon polymorph CL-20
particles having an average particle size of not greater than 10
microns.
13. The method of claim 11, wherein providing the aqueous
dispersion comprising epsilon polymorph CL-20 particles comprises
providing the aqueous dispersion comprising epsilon polymorph CL-20
particles having an average particle size in a range of 1 micron to
4 microns.
14. The method of claim 11, wherein providing the aqueous
dispersion comprising epsilon polymorph CL-20 particles comprises
providing the aqueous dispersion comprising epsilon polymorph CL-20
particles having an average particle size in a range of 1 micron to
2 microns.
15. The method of claim 11, wherein providing the aqueous
dispersion comprising epsilon polymorph CL-20 particles comprises
providing the aqueous dispersion with 100 percent of the CL-20
particles having a particle size less than 10 microns.
16. The method of claim 11, wherein providing the aqueous
dispersion comprising epsilon polymorph CL-20 particles comprises
providing the aqueous dispersion with 100 percent of the CL-20
particles having a particle size less than 4 microns.
17. The method of claim 11, wherein providing the aqueous
dispersion comprising epsilon polymorph CL-20 particles comprises
providing the aqueous dispersion having 85 weight percent to 95
weight percent of CL-20 particles.
18. The method of claim 11, wherein providing the aqueous
dispersion comprising epsilon polymorph CL-20 particles comprises
providing the aqueous dispersion having 94 weight percent to 95
weight percent CL-20 particles.
19. The method of claim 11, wherein combining the aqueous
dispersion with the lacquer comprising the plasticized binder to
form the slurry comprises combining the aqueous dispersion with the
plasticized binder that comprises cellulose acetate butyrate and
bis-dinitropropyl acetal/bis-dinitropropyl formal.
20. The method of claim 11, wherein the explosive has a shock
sensitivity under 140 cards, as measured by the NOL Card Gap Test.
Description
CROSS-REFERENCE TO RELATED APPLICATIONS
[0001] This application is a divisional of application Ser. No.
10/210,863, filed Jul. 31, 2002, pending, which claims the benefit
of priority of U.S. Provisional Application No. 60/309,386, filed
in the U.S. Patent & Trademark Office on Aug. 1, 2001, the
complete disclosure of which is incorporated herein by
reference.
BACKGROUND OF THE INVENTION
[0003] Field of the Invention: This invention relates to the field
of explosives, especially explosives having low sensitivity to
impact. More particularly, the invention is directed to
compositions loaded with high concentrations of
2,4,6,8,10,12-hexanitro-2,4,6,8,10,12-hexaazatetracyclo-
[5.5.0.0.sup.5,90.sup.3,11]dodecane, which is also known in the art
and referred to herein as HNIW and, more commonly, CL-20. This
invention is also directed to a process for making the
explosive.
[0004] State of the Art: Nitramines are highly energetic compounds
that have found acceptance in the art of explosives. Perhaps the
most common nitramines in use in the explosives art today are
1,3,5-trinitro-1,3,5-tr- iaza-cyclohexane (RDX) and
1,3,5,7-tetranitro-1,3,5,7-tetraaza-cyclooctane (HMX).
[0005] Another energetic nitramine that has found acceptance in the
art is CL-20, which has a higher energetic performance than either
RDX or HMX. The explosive composition LX-19, which is a combination
of CL-20 and ESTANE (C.sub.5.14H.sub.7.5N.sub.0.187O.sub.1.76), is
considered by many to be the current standard by which other
explosives containing CL-20 are measured. Other examples of
explosive compositions containing CL-20 as a primary energetic
filler are disclosed in U.S. Pat. No. 6,214,137, entitled "High
Performance Explosive Containing CL-20" and U.S. Pat. No.
6,217,799, entitled "Method for Making High Performance Explosive
Formulations Containing CL-20."
[0006] Although energetic performance is a crucial feature of
energetic compositions, another important performance criteria by
which explosive compositions are evaluated is shock sensitivity. An
acceptably low shock sensitivity is extremely important to avoid
accidental detonation, avoid hazardous conditions, and ensure the
safe handling, shipment, and use of the material.
[0007] One test accepted in the art for measuring shock sensitivity
is known as the Large Scale Gap Test (LSGT), in which a test
material is placed into a metal tube on top of a witness plate. A
predetermined number of PMMA (polymethylmethacrylate) cards are
placed between the top of the metal tube and a booster material,
which typically consists of 50 weight percent PETN (pentaerythritol
tetranitrate) and 50 weight percent TNT (trinitrotoluene),
available as Pentolite. The distance between the booster and the
metal tube is expressed in cards, where one card is equal to 0.0254
cm (0.01 inch), such that 100 cards equal 2.54 cm (1 inch). A card
gap measurement is the minimum number of cards required to prevent
the booster from detonating the explosive sample, so that the
sample does not blow a hole through the witness plate. Thus, the
lower the card value, the lower the shock sensitivity of the
explosive composition. The LSGT (or NOL Card Pipe Test) is more
fully described in the Joint Technical Bulletin, Navy document
number NAVSEA INST 8020.8B, Air Force technical order 11A-1-47,
Defense Logistics Agency regulation DLAR 8220.1, and Army technical
bulletin TB700-2.
[0008] LX-14, which is a combination of the more stable nitramine
HMX and ESTANE, has an NOL card gap of 193 cards. The explosives
disclosed in U.S. Pat. No. 6,214,137 and U.S. Pat. No. 6,217,799
exhibited similar shock sensitivities to LX-14.
BRIEF SUMMARY OF THE INVENTION
[0009] The present invention provides an explosive composition
having excellent energetic performance, yet shock sensitivity that
is superior to that of the current CL-20 standard, LX-19.
[0010] Further, the present invention provides a method for
preparing the explosive composition of this invention.
[0011] In accordance with the present invention, as embodied and
broadly described in this document, an explosive composition
according to one aspect of the invention comprises a high loading
of 85 weight percent to about 96 weight percent
2,4,6,8,10,12-hexanitro-2,4,6,8,10,12-hexaazatetr-
acyclo[5.5.0.0.sup.5,90.sup.3,11]-dodecane (CL-20) and about 4
weight percent to 15 weight percent of a plasticized binder. The
CL-20 particles are fine, meaning that the particles have an
average particle size of not greater than 30 microns, more
preferably an average particle size of not greater than 10 microns,
still more preferably an average particle size of 1 micron to 4
microns, and still more preferably an average particle size of 1
micron to 2 microns.
[0012] In a particularly preferred aspect of the invention,
substantially all of the particles are fine. More specifically, 100
percent of the CL-20 particles have a particle size less than 30
microns, more preferably 100 percent of the CL-20 particles have a
particle size less than 10 microns, and still more preferably 100
percent of the CL-20 particles have a particle size less than 4
microns.
[0013] The inventors have discovered that even with a very high
CL-20 loading of at least 85 weight percent, using a very fine
distribution of CL-20 particles surprisingly reduces shock
sensitivity of the explosive well below conventional CL-20
explosives containing bimodal and multimodal distributions of fine
and coarse particles. In a particularly preferred embodiment of the
invention, the shock sensitivity is reduced to under 140 cards, as
measured by the NOL Card Gap Test.
[0014] In one particularly preferred embodiment of the invention,
the fine CL-20 particles constitute 85 weight percent to 95 weight
percent of the total composition weight and, more preferably, 94
weight percent to 95 weight percent of the total composition
weight.
[0015] In another preferred embodiment, the plasticized binder
comprises cellulose acetate butyrate and bis-dinitropropyl
acetal/bis-dinitropropyl formal.
[0016] In accordance with another aspect of the invention, the
explosive composition comprises 85 weight percent to about 96
weight percent nitramine based on the total composition weight,
with at least 80 weight percent of the total composition weight
comprising
2,4,6,8,10,12-hexanitro-2,4,6,8,10,12-hexaazatetracyclo[5.5.0.0.sup.5,90.-
sup.3,11]-dodecane (CL-20) particles having an average particle
size not greater than 30 microns, more preferably not greater than
10 microns, and still more preferably 1 micron to 4 microns. About
4 weight percent to 15 weight percent of the explosive composition
comprises a plasticized binder.
[0017] In accordance with another aspect of the invention, a method
for preparing an explosive is provided. The method comprises
combining
2,4,6,8,10,12-hexanitro-2,4,6,8,10,12-hexaazatetracyclo[5.5.0.0.sup.5,90.-
sup.3,11]-dodecane (CL-20) particles having an average particle
size not greater than 30 microns with a plasticized binder to form
an explosive composition. The explosive composition is granulated
to form the explosive, which comprises 85 weight percent to about
96 weight percent of the CL-20 particles and about 5 weight percent
to 15 weight percent of the plasticized binder.
[0018] Another aspect of the invention is provided in which an
explosive is prepared by providing an aqueous dispersion comprising
epsilon polymorph CL-20 particles having an average particle size
not greater than 30 microns, more preferably not greater than 10
microns, and still more preferably 1 micron to 4 microns. The
aqueous dispersion is combined with a lacquer comprising a
plasticized binder to form a slurry, which is agitated and from
which solvent is removed to form coated granules. The coated
granules are dried to provide an explosive having a high load of 85
weight percent to about 96 weight percent CL-20 and about 5 weight
percent to 15 weight percent of the plasticized binder.
[0019] Additional aspects and advantages of the invention will be
set forth in the description of the preferred embodiments and
methods that follows and, in part, will be apparent from the
description or may be learned by practice of the invention. The
aspects and advantages of the invention may be realized and
obtained by means of the instrumentalities and combinations pointed
out in the appended claims.
BRIEF DESCRIPTION OF THE SEVERAL VIEWS OF THE DRAWINGS
[0020] The accompanying drawings are incorporated in and constitute
a part of the specification. The drawings, together with the
general description given above and the detailed description of the
preferred embodiments and methods given below, serve to explain the
principles of the invention. In such drawings:
[0021] FIG. 1 is a schematic of one example of a slurry emulsion
process suitable for preparing the inventive explosive
composition;
[0022] FIG. 2 is a schematic sectional view of a jacketed mixer
suitable for use in the process illustrated in FIG. 1; and
[0023] FIG. 3 is a graph of an exemplary particle size distribution
of CL-20 particles in accordance with an embodiment of the
invention.
DETAILED DESCRIPTION OF THE INVENTION
[0024] Reference will now be made in detail to the presently
preferred embodiments and methods of the invention as described
below. It should be noted, however, that the invention in its
broader aspects is not limited to the specific details,
representative devices and methods, and examples described in this
section in connection with the preferred embodiments and methods.
The invention, according to its various aspects, is particularly
pointed out and distinctly claimed in the attached claims read in
view of this specification, and appropriate equivalents.
[0025] It is to be noted that, as used in the specification and the
appended claims, the singular forms "a," "an," and "the" include
plural referents unless the context clearly dictates otherwise.
[0026] In accordance with one preferred embodiment of this
invention, an explosive composition is provided that comprises 85
weight percent to about 96 weight percent
2,4,6,8,10,12-hexanitro-2,4,6,8,10,12-hexaazatetr-
acyclo[5.5.0.0.sup.5,90.sup.3,11]-dodecane (CL-20) and about 4
weight percent to 15 weight percent of a plasticized binder.
[0027] The production of CL-20 is well known in the art and is
described in various publications, including WO 00/52011. U.S. Pat.
No. 5,874,574 teaches the crystallization of CL-20 into its epsilon
polymorph. In the context of preferred embodiments of this
invention, epsilon-polymorph CL-20 is selected, although the
presence of small and expected amounts of impurities (e.g., other
CL-20 polymorphs) are acceptable and within the scope of the
preferred embodiments of the invention.
[0028] The CL-20 particles of this invention are fine, meaning that
they have an average particle size of not more than 30 microns,
preferably not more than 10 microns, and more preferably the
average particle size is 1 micron to 4 microns. It is especially
preferred that the average particle size be 1 micron to 2 microns.
Average sizes of CL-20 particles may be determined by use of a
Microtrac instrument available from Microtrac, Inc., previously
available from Leeds & Northrup, as part SRA-150. It is
preferred that 100 percent of the CL-20 particle distribution in
the composition is less than 30 microns, more preferably 100 weight
percent of the CL-20 particles is less than 10 microns, and still
more preferably 100 weight percent of the CL-20 particle
distribution is less than 4 microns in particle size. One
particularly preferred particle size distribution of about 2
microns is shown in FIG. 3.
[0029] The incorporation of other nitramines into the explosive
composition is optional. Exemplary nitramines that can be used with
CL-20 for this invention include, by way of example,
1,3,5-trinitro-1,3,5-triaz- a-cyclohexane (RDX),
1,3,5,7-tetranitro-1,3,5,7-tetraaza-cyclooctane (HMX), and
4,10-dinitro-2,6,8,12-tetraoxa-4,10-diazatetracyclo-[5.5.0.0..-
sup.5,90.sup.3,11]-dodecane (TEX). However, the fine CL-20
particles account for at least 80 weight percent of the explosive
composition when other nitramines are used, with the total
nitramine content at 85 weight percent to about 96 weight
percent.
[0030] The plasticized binder comprises at least one plasticizer
and at least one binder component, which is preferably a polymer.
Exemplary polymeric binder components are nonenergetic and include
at least one of the following: cellulose acetate butyrate (CAB),
nylon, HYTREL.RTM.8184 (polybutylene phthalate available from I. E.
DuPont Nemours & Company), PEBAX.RTM. (polyether block amide
available from ELF Atochem of Philadelphia, Pa.), and fluorocarbons
such as FLUOREL.RTM. from 3M. The nylon binder may be, for example,
6-polyamide, 6,6-polyamide, 11-polyamide, 1,2-polyamide, or any
copolymer or blend thereof.
[0031] Representative plasticizers include isodecyl pelargonate
(IDP), bis-dinitropropyl acetal and bis-dinitropropyl formal
(BDNPA/F), and glycidyl azide polymer (GAP). In the event that
BDNPA/F is selected as the plasticizer, the weight ratio of
bis-dinitropropyl acetal to bis-dinitropropyl formal is preferably
between about 45:55 and about 55:45, and more preferably is about
50:50. The plasticizer is preferably a liquid.
[0032] A preferred plasticized binder according to this invention
comprises a combination of CAB and BDNPA/F, preferably in a weight
ratio of 40:60.
[0033] Among the additives that may be included in the composition
are metals such as aluminum, boron, and magnesium.
[0034] In one preferred embodiment, the composition comprises about
94 weight percent to about 95 weight percent CL-20 particles having
an average particle size in a range of 1 to 4 microns, about 2
weight percent to about 2.8 weight percent CAB, and about 3.2
weight percent to about 4 weight percent BDNPA/F. In a still more
preferred embodiment, the composition comprises about 94 weight
percent CL-20 having an average particle size of 1 micron to 4
microns, about 2.4 weight percent CAB, and about 3.6 weight percent
BDNPA/F. In view of the large surface area of the fine CL-20
particles, it was particularly surprising that the fine CL-20
particles in high loadings of 94 to 95 weight percent could be
effectively coated with the plasticized binder.
[0035] The explosive is preferably sufficiently pressable or
extrudable to permit its formation into grains and billets suitable
for ordnance and similar applications. The principles of the
present invention outlined above are applicable to making a variety
of explosive articles but have particular applicability to the
formation of pressed or injection-loaded ordnances such as
grenades, land mines, missile warheads, and demolition
explosives.
[0036] An exemplary water slurry process for making the explosive
of this invention will be described below. It should be understood
that this invention is not limited to the described process;
rather, other methods and processes may be practiced within the
scope of this invention.
[0037] Referring now more particularly to FIG. 1, there is shown a
batchwise process for preparing the explosive of this invention.
The process may be conducted at or near room temperature. In the
illustrated process, a polymer and plasticizer from which the
plasticized binder is comprised are charged from separate tanks 10
and 12 into a lacquer mixing vessel 14 equipped with stirrer 16.
For purposes of illustration, the stirrer 16 is depicted as an
impeller. Although not shown, as an alternative, the plasticized
binder components may be premixed and charged from a single
tank.
[0038] Solvent is fed to the lacquer mixing vessel 14 from storage
tank 18. Representative solvents that may be used in this process
include one or more of the following: low molecular weight
hydrocarbons, such as straight chain hydrocarbons (e.g., hexane and
heptane) and cyclic hydrocarbons (e.g., cyclohexane and
cycloheptane); low molecular weight alcohols, such as methanol,
ethanol, propanol, isopropanol, and butanol; and esters such as
ethyl acetate. Ethyl acetate is currently the preferred solvent for
this process.
[0039] Although not shown, a stabilizer may be added to the lacquer
mixing vessel 14. Representative stabilizers include diphenyl amine
and n-alkyl nitroanilines, in which the n-alkyl group may be, for
example, methyl, ethyl, and other low molecular weight moieties
such as isopropyl.
[0040] Surfactants may also be added into the jacketed mixer 20.
Suitable surfactants include, by way of example, low molecular
weight alcohols, such as 1-butanol and isopropyl alcohol. It has
been found that 1-butanol has synergistic effects with CL-20 in
regard to its defoaming capability. The amount of surfactant
introduced into the process should be sufficient to reduce foaming
and produce a yield of at least 99 weight percent.
[0041] An aqueous dispersion is prepared by charging CL-20 from
storage tank 22 and water from tank 24 into a jacketed mixer 20
equipped with stirrer 26, which is depicted as an impeller. Then,
the lacquer from mixing vessel 14 is fed into the jacketed mixer 20
to form CL-20 granules and precipitate the plasticized binder on
the CL-20 granules. The granules begin to take shape as the lacquer
is added to the jacketed mixer 20 and have, for the most part,
taken their final form by the time the lacquer addition is
completed. Referring to FIG. 2, during stirring of the granules an
air sweep may be passed through the jacketed mixer 20. The air
sweep removes solvent, surfactant, and water from the jacketed
mixer 20 through vent 28. The granules may then be further rinsed
with water while stirring is continued to prevent unacceptable
amounts of agglomeration.
[0042] The amount of water fed into the jacketed mixer 20 should
sufficiently dilute the lacquer from mixing vessel 14, thereby
preventing granules from sticking to the walls of the jacketed
mixer 20 and agglomerating. On the other hand, if too much water is
added to the jacketed mixer 20, the growth rate of the granules may
be impeded, resulting in small and highly sensitive granules.
Generally, the weight ratio of CL-20 to water may be about 2.5:1 to
about 4.5:1 and, more preferably is about 3:1.
[0043] The amount of solvent fed into the jacketed mixer 20 should
be sufficient to facilitate mixing and dilution of the CL-20.
However, excess solvent may cause a significant amount of the CL-20
to dissolve and may add significant cost towards minimizing
environmental impact of waste streams. Generally, the amount of
solvents used in the process depends upon many variables, including
the solvent selected, the concentration of CL-20, and the
plasticized binder selected. When viewed in reference to this
disclosure, ascertaining suitable solvent concentrations is within
the purview of those of ordinary skill in the art without undue
experimentation. By way of example, the weight ratio of water to
ethyl acetate may be about 6.3:1 for a CL-20 concentration of 90
weight percent and 9.6:1 for a CL-20 concentration of 94 weight
percent.
[0044] The addition rate of the lacquer to the CL-20 aqueous
dispersion may be selected to facilitate the formation of round and
hard CL-20 granules. Due to the large surface areas of the fine
CL-20 particles, lacquer is preferably added quickly to ensure
coating. Preferably, the granular agglomerates are from about 0.85
mm to about 4 mm in size. The temperature at which the process is
conducted is dependent upon the solvent and, in particular, should
not be higher than the boiling point of the solvent. Also, the
temperature should be maintained within reasonable limits to avoid
polymorph conversion of the CL-20, which preferably remains as
epsilon polymorph throughout the process. The temperature may be
within a range of from about 30.degree. C. to about 50.degree. C.,
and more preferably may be room temperature. Generally, the steps
of combining the CL-20 aqueous dispersion with the lacquer and
agitating are conducted at a sufficiently low temperature and the
solvent is present in a sufficiently low concentration to avoid
significant polymorph conversion of the epsilon-polymorph
CL-20.
[0045] The granules formed in the jacketed mixer 20 and water are
poured on a primary filter 30 for drying. The granules are then
passed to an oven or dryer 32 and spread out and subjected to a
vacuum for at least about 24 hours at, for example, about
49.degree. C. to 54.degree. C. Excess solvent is passed to waste
tank 34. Although not shown in the figures, for larger scale
processes, a secondary recovery system (e.g., filters, vacuum
collection tanks, heat exchangers, and the like) may be used.
[0046] The following examples serve to explain embodiments of the
invention in more detail. These examples are not to be construed as
being exhaustive or exclusive as to the scope of this
invention.
[0047] The CL-20 used in the examples and comparative examples was
of the epsilon polymorph type. The CL-20, supplied by ATK Thiokol
Propulsion Corp. of Promontory, Utah, was crystallized using a
nonchlorinated solvent process as described in U.S. Pat. No.
5,874,574, the complete disclosure of which is incorporated herein
by reference. The particles were subjected to dry grinding in a
fluid energy mill to give their desired size as the feed stock.
EXAMPLES
[0048] Example 1 was prepared as follows: 478 grams of CAB were
dissolved in 6100 grams of ethyl acetate. 750 grams of BDNPA/F were
stirred into the CAB solution to provide a lacquer with the
plasticized binder. CL-20 particles having a distribution shown in
FIG. 3 were slurried in 1.5 gallons of water and 375 grams of
n-butanol. A 20 gallon slurry mixer was then charged with 8.5
gallons of water, and the water temperature was maintained at
90.degree. F. to 95.degree. F. The slurried CL-20 was then added to
the slurry mixer operating at an impeller rate of 450 rpm. 0.5 to
1.0 gallons of water were then added to the slurry mixer, then 1000
grams of n-butanol were added. The blower was started at 50%
capacity to draw air over the slurry in the slurry mixer. The
impeller rate was then increased to 1150 rpm, and 75% of the
lacquer containing the plasticized binder was added over a
three-minute period. The blower was increased to 100% capacity and
the impeller rate was adjusted to form and mix the granules. The
remaining 25% of the lacquer was then added over a 25-minute
period. Fifteen minutes after the lacquer had been added, 200 grams
of ethyl acetate were added. Ten minutes later, 5 gallons of water
were added and the granules were removed from the mixer through a
bottom valve and screened.
[0049] The following examples were prepared using the water slurry
process described above and illustrated in the accompany figures.
For Example 2, CL-20 particles having a size distribution shown in
FIG. 3 were used. Comparative Examples A and B used a combination
of fine CL-20 particles with larger coarse particles of 70 microns
to 350 microns. In Comparative Example A, 90 weight percent of the
CL-20 particles were fine (having the distribution of FIG. 3) and
10 weight percent of the CL-20 particles were coarse. Comparative
Example B used 95 weight percent fine CL-20 (having the
distribution of FIG. 3) and 5 weight percent coarse CL-20
particles. Each of Example 2 and Comparative Examples A and B had a
90 weight percent CL-20 concentration and a 10 weight percent
plasticized binder of CAB and BDNPA/F.
[0050] The NOL card gap number of Example 2 was found to be about
137. On the other hand, Comparative Examples A and B both detonated
at 140 cards, 150 cards, and 160 cards. These results indicate that
even with just 5 weight percent large CL-20 particles, the shock
sensitivity was increased greatly.
[0051] The foregoing detailed description of the preferred
embodiments of the invention has been provided for the purposes of
illustration and description and is not intended to be exhaustive
or to limit the invention to the precise embodiments disclosed. The
embodiments were chosen and described in order to best explain the
principles of the invention and its practical application, thereby
enabling others skilled in the art to understand the invention for
various embodiments and with various modifications as are suited to
the particular use contemplated. It is intended that the scope of
the invention cover various modifications and equivalents included
within the spirit and scope of the appended claims.
* * * * *