TECHNICAL FIELD
[0001] This invention relates to an explosive composition and an explosive composition shaped
body as well as a method for producing the same, and concretely to an explosive composition
suitable for use in a gas generator for actuating an automobile safety device such
as an air bag, a seat belt pretensioner, a bonnet lifting device or the like.
RELATED ART
[0002] As the explosive composition for the gas generator, there are, for example, a gas
generating agent, an enhancing agent, a priming composition, an autoiginition agent
and so on. Among them, the gas generating agent, the enhancing agent and the autoignition
agent are typically used as a shaped body, so that they are added with an adhesive
(binder) dissolving in a solvent used such as water, an organic solvent or the like
(
JP-A-2000-95592). Also, there is known an extrusion-moldable priming composition using a water-soluble
or water-expandable binder as an aqueous adhesive using water as a solvent (
JP-A-2003-524565). Furthermore, there is known an explosive composition using an aqueous suspension
of ethylene/vinyl acetate copolymer as an aqueous adhesive (
JP-A-2003-238285). And also, there is known an explosive composition using a synthetic hydrotalcite
as an inorganic binder (
JP-A-2001-192288).
DISCLOSURE OF THE INVENTION
[0003] However, in case of the binder using the organic solvent as a solvent as disclosed
in
JP-A-2000-95592, there are drawbacks that it is necessary to take a care on the safeness and the
regulation of emitting VOC (volatile organic compounds) should be satisfied. In case
of the binder using water as a solvent as disclosed in
JP-A-2000-95592 or
JP-A-2003-524565, the safeness is good, but there are drawbacks that the hygroscopicity can not be
lowered and the shaped bodies after shaping are fixed to each other. Furthermore,
there are many problems in the production such as time-consuming cleaning due to the
adhesion of chemicals to the shaping machine and the like. And also, there is a problem
in the maintenance of the production device requiring a solvent for cleaning the shaping
machine due to the adhesion of chemicals. In the composition as disclosed in
JP-A-2003-238285, the shaped body can not be obtained even by the extrusion molding. The binder used
in
JP-A-2001-192288 is effective as a binder for tablet machinery, but is not suitable as a binder for
extrusion molding and hence the extrusion-molded body can not be obtained.
[0004] The invention is made for solving the above problems and is to provide an explosive
composition and an explosive composition shaped body which are good in the water resistance
and less in the production problem as compared with the conventional ones. Also, it
is another object of the invention to provide a method of producing the explosive
composition and the explosive composition shaped body.
[0005] That is, the summary and construction of the invention are as follows.
[0006] 1. An explosive composition characterized by milling and drying a fuel component
and an oxidizer component in the presence of an aqueous emulsion of a hydrophobic
tackifier.
[0007] 2. The explosive composition according to the item 1, wherein a content of the hydrophobic
tackifier is 2-15 mass%.
[0008] 3. The explosive composition according to the item 1 or 2, wherein the hydrophobic
tackifier is at least one selected from the group consisting of a rubber-based tackifier,
an acryl-based tackifier and a silicone-based tackifier.
[0009] 4. The explosive composition according to the item 3, wherein the hydrophobic tackifier
is an acryl-based tackifier.
[0010] 5. The explosive composition according to the item 3 or 4, wherein the hydrophobic
tackifier has a heat decomposition temperature of not lower than 200°C.
[0011] 6. The explosive composition according to any one of the items 1-5, wherein the fuel
component is a nitrogen-containing compound and/or boron.
[0012] 7. The explosive composition according to the item 6, wherein the nitrogen-containing
compound is at least one selected from the group consisting of guanidine, tetrazole,
bitetrazole, triazole, hydrazine, triazine, azodicarbonamide, dicyanamide and derivatives
thereof and a nitramine compound.
[0013] 8. The explosive composition according to any one of the items 1-7, wherein the oxidizer
component is at least one selected from the group consisting of a chlorate, a perchlorate,
a nitrate and a basic nitrate.
[0014] 9. The explosive composition according to the item 8, wherein the oxidizer component
is at least one selected from the group consisting of ammonium perchlorate, potassium
perchlorate, sodium perchlorate, potassium nitrate, sodium nitrate, strontium nitrate
and basic copper nitrate.
[0015] 10. The explosive composition according to any one of the items 1-9, which further
contains at least one selected from a metallic powder, silicon nitride and a metal
nitride.
[0016] 11. The explosive composition according to any one of the items 1-10, which further
contains a surfactant.
[0017] 12. The explosive composition according to the item 11, wherein the surfactant is
a nonionic surfactant having a HLB value of not more than 15.
[0018] 13. An explosive composition shaped body characterized by milling, shaping and drying
a fuel component and an oxidizer component as described in any one of the items 1-9
in the presence of an aqueous emulsion of a hydrophobic tackifier.
[0019] 14. The explosive composition shaped body according to the item 13, wherein the shaped
body is any of a gas generating agent, an autoignition agent and an enhancer agent.
[0020] 15. The explosive composition shaped body according to the item 13 or 14, wherein
the shaped body is for an automotive safety device.
[0021] 16. The explosive shaped body according to any one of the items 13-15, wherein the
shaped body has any of a granular form, a tablet form, a columnar form, a cylindrical
form, a prismatic form, a porous cylindrical form and a porous prismatic form.
[0022] 17. The explosive composition shaped body according to any one of the items 13-16,
which further contains at least one selected from a metallic powder, silicon nitride
and a metal nitride.
[0023] 18. The explosive composition shaped body according to any one of the items 13-17,
which further contains a surfactant.
[0024] 19. The explosive composition shaped body according to the item 18, wherein the surfactant
is a nonionic surfactant having a HLB value of not more than 15.
[0025] 20. A method of producing an explosive composition, which comprises milling a fuel
component and an oxidizer component with an aqueous emulsion of a hydrophobic tackifier
and drying them.
[0026] 21. A method of producing an explosive composition shaped body, which comprises milling
a fuel component and an oxidizer component with an aqueous emulsion of a hydrophobic
tackifier and shaping, drying and solidifying them.
[0027] 22. The method of producing an explosive composition shaped body according to the
item 17, wherein the shaping is an extrusion molding.
[0028] The explosive composition according to the invention is less in the adhesion of mutual
shaped bodies after the shaping and easy in the disintegration of aggregated chemicals
after the drying. Also, the resulting dry shaped body is good in the moisture absorption
resistance and water resistance and suitable as an explosive composition for a gas
generator actuating a moisture-proof automobile safety device. Furthermore, in the
production of the explosive composition shaped body according to the invention, the
hydrophobic tackifier is dispersed into water at an emulsion state for use as an aqueous
emulsion, whereby the milled mass of the fuel component and oxidizer component becomes
glutinous and facilitates the extrusion molding. Moreover, the milled mass hardly
adheres to the production machine and also the cleaning of the machine after the production
becomes easy.
BEST MODE FOR CARRYING OUT THE INVENTION
[0029] The explosive composition according to the invention is obtained by using a fuel
component and an oxidizer component as an essential component and milling them with
an aqueous emulsion of a hydrophobic tackifier and shaping, if necessary, and then
drying. The tackifier used in the invention is a hydrophobic tackifier and forms an
aqueous emulsion by dispersing into water. As the hydrophobic tackifier are mentioned,
for example, a rubber-based tackifier, an acryl-based tackifier and a silicone-based
tackifier, but the acryl-based tackifier is preferable from a viewpoint of the burning
rate and the cleanability of combustion gas. The amount of the tackifier used is preferable
to be 2-15 mass% as a solid content in the explosive composition, and is more preferable
to be 3-9 mass% as a solid content from a view point of the shapability and the cleanability
of combustion gas. The heat decomposition temperature of the tackifier is desirable
to be higher than a self-decomposition temperature of the explosive composition and
is preferable to be not lower than 200°C. Moreover, it is preferable to use the acryl-based
tackifier so as to render the explosive composition before the shaping into a glutinous
state in view of the extrusion molding.
[0030] As the fuel component used in the invention may be mentioned a nitrogen-containing
compound and boron. As the nitrogen-containing compound may be mentioned at least
one selected from the group consisting of guanidine, tetrazole, bitetrazole, triazole,
hydrazine, triazine, azodicarbonamide, dicyanamide and derivatives thereof and a nitramine
compound. More concretely, there may be mentioned 5-oxo-1,2,4-triazole, tetrazole,
5-aminotetrazole, nitric acid aminotetrazole, nitroaminotetrazole, bitetrazole (5,5'-bi-1H-tetrazole),
5,5'-bi-1H-tetrazole diammonium salt, azobistetrazole, 5,5'-azotetrazole diguanidine
salt, guanidine, nitroguanidine, cycanoguanidine, triaminoguanidine nitrate, guanidine
nitrate, aminoguanidine nitrate, biuret, azodicarbonamide, carbohydrazide, carbohydrazide
nitrate complex, oxalic acid hydrazide, hydrazine nitrate complex, anmine complex
and so on. Among these nitrogen-containing compounds, one or more selected from the
tetrazole derivatives and guanidine derivatives are preferable in view that they are
cheap and good in the reactivity and relatively easy in the handling, and particularly
one or more selected from nitroguanidine, guanidine nitrate, bitetrazole, azobistetrazole
and 5-aminotetrazole are preferable.
[0031] The content of the fuel component (compounding ratio) in the explosive composition
according to the invention is preferably about 15-50 mass%, more preferably about
20-45 mass%. When the content of the fuel component (compounding ratio) is less than
15 mass%, there is a tendency that when the explosive composition is used as a gas
generating agent, the mole number of the gas generated per 100 g of the explosive
composition decreases and the amount of NOx generated increases due to oxygen excess.
While, when the content of the fuel component (compounding ratio) exceeds 50 mass%,
the fuel component having a low specific gravity becomes large and hence the true
specific gravity of the explosive composition as the gas generating agent reduces
to decrease the filling amount per volume of the gas generator for an air bag, a sheet
belt pretensioner or the like. And also, the oxidizer component is lacking and hence
the generation of CO gas tends to be increased. When the nitrogen-containing compound
is used together with boron as the fuel component, the ratio of boron used per 1 part
by mass of the nitrogen-containing compound is preferably 0.1-10 parts by mass, more
preferably 0.5-5 parts by mass.
[0032] As the oxidizer component used in the invention are mentioned, for example, chlorates,
perchlorates, nitrates and basic nitrates. The chlorate includes, for example, an
alkali metal salt of chloric acid such as potassium chlorate, sodium chlorate or the
like; an alkaline earth metal salt of chloric acid such as barium chlorate, calcium
chlorate or the like; and an ammonium salt of chloric acid such as ammonium chlorate
or the like. The perchlorate includes, for example, an alkali metal salt of perchloric
acid such as potassium perchlorate, sodium perchlorate or the like; an alkaline earth
metal salt of perchloric acid such as barium perchlorate, calcium perchlorate or the
like; and an ammonium salt of perchloric acid such as ammonium perchlorate or the
like. The nitrate includes, for example, an ammonium salt of nitric acid such as ammonium
nitrate or the like; an alkali metal salt of nitric acid such as sodium nitrate, potassium
nitrate or the like; an alkaline earth metal salt of nitric acid such as barium nitrate,
strontium nitrate or the like; and so on. As the basic nitrate are mentioned, for
example, basic copper nitrate, basic manganese nitrate, basic iron nitrate, basic
molybdenum nitrate, basic bismuth nitrate, basic cerium nitrate and so on. Among them,
the perchlorate, nitrate or basic nitrate is preferable. Among the perchlorates is
preferable ammonium perchlorate or potassium perchlorate which is large in the amount
of the gas generated and high in the reactivity. Among the nitrates is preferable
a nitrate of a metal selected from alkali metals and alkaline earth metals from a
viewpoint of the reactivity and handling property, and particularly potassium nitrate
and strontium nitrate are preferable. Among the basic nitrates is preferable basic
copper nitrate which is low in the burning temperature and good in the heat stability.
[0033] The content of the oxidizer component (compounding ratio) in the explosive composition
according to the invention is preferably about 40-80 mass%. When the content of the
oxidizer component (compounding ratio) is less than 40 mass%, oxygen is lacking and
the occurrence of CO gas tends to be increased, while when it exceeds 80 mass%, there
is a tendency of increasing the amount of NOx generated due to oxygen excess.
[0034] Further, the explosive composition according to the invention may contain metallic
powder, a silicon nitride or a metal nitride for increasing the burning rate and more
improving the ignition characteristic. As the metallic powder are mentioned, for example,
aluminum, magnesium, magnarium, titanium, zirconium and the like. As the silicon nitride
or metal nitride are mentioned, for example, silicon nitride, boron nitride, aluminum
nitride, magnesium nitride, molybdenum nitride, tungsten nitride, calcium nitride,
barium nitride, strontium nitride, zinc nitride, sodium nitride, copper nitride, titanium
nitride, manganese nitride, vanadium nitride, nickel nitride, cobalt nitride, iron
nitride, zirconium nitride, chromium nitride, tantalum nitride, niobium nitride, cerium
nitrides, scandium nitride, yttrium nitride, germanium nitride and the like. The content
of the metallic powder, silicon nitride or metal nitride in the explosive composition
is preferable to be 0-10 mass%.
[0035] In the explosive composition according to the invention may be further included a
surfactant for increasing the milling property of the fuel component, oxidizer component
and hydrophobic tackifier and more enhancing the extrusion moldability. As the surfactant
may be used any of nonion surfactants, anion surfactants and cation surfactants, but
the nonion surfactant such as NOIGEN (made by Dai-ichi Kogyo Seiyaku Co., Ltd.) or
the like is desirable. In the nonion surfactant, HLB (Hydrophile Lipophile Balance)
value is preferable to be not more than 15. More preferably, it is 3-15. In case of
using two or more surfactants, the HLB value is calculated on weighted mean. When
the HLB value is too low, the dispersing ability in water system is poor, while when
it is too high, the moisture absorption resistance of the explosive composition lowers.
The content of the surfactant in the explosive composition is preferably 0-5 mass%.
[0036] In the explosive composition according to the invention may be further included an
extrusion assistant as a water retaining agent-lubricant for improving the extrusion
property. As the extrusion assistant are mentioned carboxymethyl cellulose (CMC),
sodium salt of carboxymethyl cellulose (CMCNa), potassium salt of carboxymethyl cellulose,
ammonium salt of carboxymethyl cellulose, cellulose acetate, cellulose acetate butyrate
(CAB), methylcellulose (MC), ethylcellulose (EC), hydroxypropyl methylcellulose (HPMC),
hydroxyethylcellulose (HEC), ethylhydroxy ethylcellulose (EHEC), hydroxypropylcellulose
(HPC), carboxymethylethyl cellulose (CMEC) and the like. The content of the extrusion
assistant is preferable to be 0-1 mass% in the explosive composition.
[0037] A slug-forming agent such as acid clay, kaolin or the like, a chlorine-neutralizing
agent such as an alkali metal, an alkaline earth metal or the like, a burning catalyst
such as molybdenum oxide, vanadium oxide, iron oxide, copper oxide, chromium oxide,
cobalt oxide, aluminum oxide or the like, and so on may be compounded, if necessary.
[0038] The explosive composition according to the invention is preferable to be used as
a shaped body. The shaped body of the explosive composition can be used as a gas generating
agent, an autoignition agent or an enhancer agent. In case of the gas generating agent,
it is preferable to use the nitrogen-containing compound as the fuel. The enhancer
agent is used for enlarging a flame produced from an exploder to easily burn the gas
generating agent, in which the nitrogen-containing compound or boron is preferable
as the fuel. The autoignition agent has a nature of self-igniting at a temperature
lower than the ignition temperature of the gas generating agent such as about 180°C,
and the use of 5-aminotetrazole, alkali metal salt of nitric acid or molybdenum trioxide
is mentioned (see
JP-A-2001-80986).
[0039] Also, the explosive composition shaped body according to the invention is used, for
example, in parts for automobile safety device. As the part for automobile safety
device are mentioned, for example, a gas generator for an air bag, a gas generator
for a sheet belt pretensioner, and a small-size gas generator for a bonnet lifting
device. The explosive composition shaped body according to the invention is used in
these gas generators in combination with the gas generating agent, autoignition agent
and enhancer agent, if necessary.
[0040] The explosive composition shaped body according to the invention takes on a powdery
or granular form. As the form of the shaped body are mentioned an extrusion molded
body and a tablet. As the form of the extrusion molded body are mentioned a granular
form, a columnar form, a cylindrical form, a prismatic form, a porous cylindrical
form, a porous prismatic form and the like. As the tablet are mentioned a tablet pellet
and the like.
[0041] The explosive composition according to the invention is produced by milling and drying
the fuel component and the oxidizer component with the aqueous emulsion of the hydrophobic
tackifier. At this moment, the aforementioned metallic powder, silicon nitride, metal
nitride, surfactant, extrusion assistant, burning catalyst and the like may be properly
selected and compounded within a range not damaging the object of the invention in
addition to the above components. Also, in the production of the explosive composition
shaped body according to the invention, the fuel component and the oxidizer component
may be milled with the aqueous emulsion of the hydrophobic tackifier and shaped and
then dried and solidified. In this case, it is preferable that the milled mass obtained
by milling the components is shaped in a shaping machine, and also the mixing and
milling may be carried out in the shaping machine, particularly an extruder. As the
shaping machine are mentioned, for example, a tableting machine, a compression shaping
machine, an extrusion molding machine, a swaging machine, a granulating machine and
the like. Among them, the extrusion molding machine is preferable.
<<EXAMPLES>>
[0042] The invention will be further described in detail with reference to examples, but
the invention is not limited to the following examples.
(Example 1)
[0043] In a rocking mixer are mixed 40 mass% of guanidine nitrate, 25 mass% of strontium
nitrate and 25 mass% of basic copper nitrate, which are then mixed with 9 mass% as
a solid content of an aqueous emulsion of an acryl-based tackifier and 1 mass% of
a surfactant, NOIGEN TDS-30 (made by Dai-ichi Kogyo Seiyaku Co., Ltd.) having an HLB
value of 8.0 in a milling machine and further 15 parts by mass of a deionized water
is added per 100 parts by mass of the above component system to conduct uniform milling.
Then, the resulting milled mass is extruded into a predetermined shape through a dice
of 2.5 mm in diameter of an extruder under a given pressure. The extrusion molded
body of the explosive composition is cut at a length of 6.5 mm, which is dried to
obtain an explosive composition shaped body for a columnar gas generating agent.
[0044] In the resulting explosive composition shaped body for the gas generating agent,
a burning rate (40%-70%) dp/dt as a parameter indicating the ignitability and combustibility
is 2.32 MPa/ms. The burning rate (40%-70%) dp/dt means a gradient of a curve arriving
from 40% to 70% when a maximum pressure is 100% as determined from a combustion curve
between burning time and burning pressure by measuring a pressure inside a bomb through
a pressure sensor when 0.3 g of an enhancer agent and 2.5 g of a gas generating agent
are burnt in the bomb of 18 cc.
(Example 2)
[0045] In a rocking mixer are mixed 40 mass% of guanidine nitrate, 25 mass% of strontium
nitrate, 25 mass% of basic copper nitrate and 1 mass% of hydroxypropyl methylcellulose,
which are then mixed with 8 mass% as a solid content of an aqueous emulsion of an
acryl-based tackifier in a milling machine and further 15 parts by mass of a deionized
water is added per 100 parts by mass of the above component system to conduct uniform
milling. Then, the resulting milled mass is extruded into a predetermined shape through
a dice of 2.5 mm in diameter of an extruder under a given pressure. The extrusion
molded body of the explosive composition is cut at a length of 6.5 mm, which is dried
to obtain an explosive composition shaped body for a columnar gas generating agent.
[0046] In the resulting explosive composition shaped body for the gas generating agent,
a burning rate (40%-70%) dp/dt as a parameter indicating the ignitability and combustibility
is 2.27 MPa/ms. The burning rate (40%-70%) dp/dt means a gradient of a curve arriving
from 40% to 70% when a maximum pressure is 100% as determined from a combustion curve
between burning time and burning pressure by measuring a pressure inside a bomb through
a pressure sensor when 0.3 g of an enhancer agent and 2.5 g of a gas generating agent
are burnt in the bomb of 18 cc.
(Example 3)
[0047] In a rocking mixer are mixed 10 mass% of 5-aminotetrazole and 68 mass% of potassium
nitrate, which are then mixed with 12 mass% of boron, 9 mass% as a solid content of
an aqueous emulsion of an acryl-based tackifier and 1 mass% of a surfactant, NOIGEN
TDS-30 (made by Dai-ichi Kogyo Seiyaku Co., Ltd.) in a milling machine and further
16 parts by mass of a deionized water is added per 100 parts by mass of the above
component system to conduct uniform milling. Then, the resulting milled mass is extruded
into a predetermined shape through a dice of 1.8 mm in diameter of an extruder under
a given pressure. The extrusion molded body of the explosive composition is cut at
a length of 2.5 mm, which is dried to obtain an explosive composition shaped body
for a columnar gas generating agent.
[0048] In the resulting explosive composition shaped body for the gas generating agent,
a burning rate (30%-70%) dp/dt as a parameter indicating the ignitability and combustibility
is 10.3 MPa/ms. The burning rate (30%-70%) dp/dt means a gradient of a curve arriving
from 40% to 70% when a maximum pressure is 100% as determined from a combustion curve
between burning time and burning pressure by measuring a pressure inside a bomb through
a pressure sensor when 0.3 g of an enhancer agent and 2.5 g of a gas generating agent
are burnt in the bomb of 18 cc.
(Example 4)
[0049] In a rocking mixer are mixed 26 mass% of ammonium perchlorate, 26 mass% of strontium
nitrate and 4 mass% of copper oxide as a burning catalyst, which are then mixed with
34 mass% of nitroguanidine, 9 mass% as a solid content of an aqueous emulsion of an
acryl-based tackifier and 1 mass% of a surfactant, NOIGEN TDS-30 (made by Dai-ichi
Kogyo Seiyaku Co., Ltd.) in a milling machine and further 13 parts by mass of a deionized
water is added per 100 parts by mass of the above component system to conduct uniform
milling. Then, the resulting milled mass is extruded into a predetermined shape through
a dice of 1.5 mm in diameter of an extruder under a given pressure. The extrusion
molded body of the explosive composition is cut at a length of 2.0 mm, which is dried
to obtain an explosive composition shaped body for a columnar gas generating agent.
[0050] In the resulting explosive composition shaped body for the gas generating agent,
a burning rate (30%-70%) dp/dt as a parameter indicating the ignitability and combustibility
is 13.1 MPa/ms. The burning rate (30%-70%) dp/dt means a gradient of a curve arriving
from 40% to 70% when a maximum pressure is 100% as determined from a combustion curve
between burning time and burning pressure by measuring a pressure inside a bomb through
a pressure sensor when 1250 mg of the explosive composition for the gas generating
agent are burnt in the bomb of 10 cc.
(Example 5)
[0051] In a rocking mixer are mixed 28 mass% of 5-aminotetrazole, 61 mass% of potassium
nitrate and 4 mass% of molybdenum trioxide, which are then mixed with 6 mass% as a
solid content of an aqueous emulsion of an acryl-based tackifier and 1 mass% of a
surfactant, NOIGEN TDS-30 (made by Dai-ichi Kogyo Seiyaku Co., Ltd.) in a milling
machine and further 16 parts by mass of a deionized water is added per 100 parts by
mass of the above component system to conduct uniform milling. Then, the resulting
milled mass is extruded into a predetermined shape through a dice of 1.8 mm in diameter
of an extruder under a given pressure. The extrusion molded body of the explosive
composition is cut at a length of 2.5 mm, which is dried to obtain an explosive composition
shaped body for a columnar autoignition agent.
[0052] In order to evaluate the performances of the resulting explosive composition shaped
body for the autoignition agent, the ignition time at 200°C and the decomposition
starting temperature through TG-DTA thermobalance/differential thermal analytical
instrument are measured. As a result, the ignition time at 200°C is 2 seconds, and
the decomposition starting temperature is 175°C.
(Example 6)
[0053] A weight reduction ratio of the explosive composition shaped body for the enhancer
agent obtained in Example 3 is measured by subjecting to a thermal shock test of repeating
a temperature change of from -40°C to 107°C by 200 cycles and to a heat-resistant
test of leaving at 107°V for 400 hours, 1500 hours or 3000 hours. Also, an internal
pressure of a bomb when 1200 mg of the explosive composition for the enhancer agent
is burnt in the bomb of 18 cc is measured to determine a relation between a burning
time and a burning pressure (30%-70%)dp/dt before and after the test. The results
are shown in Table 1. As seen from the results, there is obtained the explosive composition
for the enhancer agent in which the weight reduction ratio in the thermal shock test
and the heat-resistant test is small and the change of the burning rate is small and
the environmental resistance is good.
[0054]
Table 1
| |
Before test |
107°, 400 hours |
107°C, 1500 hours |
107°C, 3000 hours |
Thermal shock test |
| Weight reduction ratio (%) |
- |
0.08 |
0.13 |
0.26 |
0.04 |
| (30%-70%)dp/dt Burning rate MPa/ms |
10.3 |
9.8 |
8.9 |
8.3 |
8.2 |
(Example 7)
[0055] In a rocking mixer are mixed 40 mass% of guanidine nitrate, 25 mass% of strontium
nitrate and 25 mass% of basic copper nitrate, which are then mixed with 9 mass% as
a solid content of an aqueous emulsion of an acryl-based tackifier and 1 mass% of
a surfactant, NOIGEN TDS-80 (made by Dai-ichi Kogyo Seiyaku Co., Ltd.) having an HLB
value of 13.3 in a milling machine and further 15 parts by mass of a deionized water
is added per 100 parts by mass of the above component system to conduct uniform milling.
Then, the resulting milled mass is extruded into a predetermined shape through a dice
of 2.5 mm in diameter of an extruder under a given pressure. The extrusion molded
body of the explosive composition is cut at a length of 6.5 mm, which is dried to
obtain an explosive composition shaped body for a columnar gas generating agent.
(Example 8)
[0056] In a rocking mixer are mixed 40 mass% of guanidine nitrate, 25 mass% of strontium
nitrate and 25 mass% of basic copper nitrate, which are then mixed with 9 mass% as
a solid content of an aqueous emulsion of an acryl-based tackifier and 1 mass% of
a surfactant, NOIGEN TDS-200D (made by Dai-ichi Kogyo Seiyaku Co., Ltd.) having an
HLB value of 16.3 in a milling machine and further 15 parts by mass of a deionized
water is added per 100 parts by mass of the above component system to conduct uniform
milling. Then, the resulting milled mass is extruded into a predetermined shape through
a dice of 2.5 mm in diameter of an extruder under a given pressure. The extrusion
molded body of the explosive composition is cut at a length of 6.5 mm, which is dried
to obtain a composition shaped body for a columnar gas generating agent.
(Comparative Example 1)
[0057] In a rocking mixer are mixed 41 mass% of guanidine nitrate, 25 mass% of strontium
nitrate, 25 mass% of basic copper nitrate, 6 mass% of hydroxypropyl methylcellulose
and 3 mass% of polyvinyl pyrrolidone, and further 15 parts by mass of a deionized
water is added per 100 parts by mass of the above component system to conduct uniform
milling. Then, the resulting milled mass is extruded into a predetermined shape through
a dice of 2.5 mm in diameter of an extruder under a given pressure. The extrusion
molded body of the explosive composition is cut at a length of 6.5 mm, which is dried
to obtain an explosive composition shaped body for a columnar gas generating agent.
[0058] An experiment for moisture absorption is carried out with respect to the explosive
compositions for the gas generating agent obtained in Examples 1, 7, and 8 and the
composition shaped body for the gas generating agent obtained in Comparative Example
1. In this moisture absorption experiment, the explosive composition shaped body for
the gas generating agent is exposed to an atmosphere having a relative humidity of
31%, 52%, 80% or 93% at 25°C to measure a weight increase every a given time. The
results on the weight change ratio to weight before the exposure in the measured atmosphere
are shown in Table 2. From these results, it can be seen that when the examples are
compared with the comparative example as to the weight change ratio after 48 hours,
the moisture absorption is less in the examples because the weight change ratio in
the examples is 1.42% at maximum, while that in Comparative Example 1 is 1.530%. Also,
when the examples are compared with each other, it can be seen that the moisture absorption
in large as the HLB value becomes high because the weight change ratio increases in
the order that the HLB value of the nonion surfactant is 8.0 in Example 1, and the
HLB value is 13.3 in Example 7 and the HLB value is 16.3 in Example 8.
[0059]
Table 2
| Example (Comparative Example) |
Relative humidity |
Weight change ratio after 12 hours (%) |
Weight change ratio after 24 hours (%) |
Weight change ratio after 48 hours (%) |
| Example 1 |
31% |
0.035 |
0.078 |
0.144 |
| 52% |
0.130 |
0.199 |
0.265 |
| 80% |
0.198 |
0.305 |
0.423 |
| 93% |
0.313 |
0.592 |
0.681 |
| Example 7 |
31% |
0.038 |
0.081 |
0.161 |
| 52% |
0.132 |
0.210 |
0.305 |
| 80% |
0.214 |
0.370 |
0.514 |
| 93% |
0.350 |
0.780 |
0.805 |
| Example 8 |
31% |
0.064 |
0.166 |
0.17 |
| 52% |
0.161 |
0.314 |
0.355 |
| 80% |
0.247 |
0.688 |
0.83 |
| 93% |
0.516 |
1.19 |
1.42 |
| Comparative Example 1 |
31% |
0.054 |
0.158 |
0.180 |
| 52% |
0.145 |
0.291 |
0.390 |
| 80% |
0.230 |
0.508 |
0.860 |
| 91% |
0.479 |
0.718 |
1.530 |
(Comparative Example 2)
[0060] In a rocking mixer are mixed 26 mass% of ammonium perchlorate, 26 mass% of strontium
nitrate, and 4 mass% of copper oxide, 6 mass% of hydroxypropyl methylcellulose and
3 mass% of polyacrylamide as a burning catalyst, which are mixed with 35 mass% of
nitroguanidine in a milling machine and further 15 parts by mass of a deionized water
is added per 100 parts by mass of the above component system to conduct uniform milling.
Then, the resulting milled mass is extruded into a predetermined shape through a dice
of 1.5 mm in diameter of an extruder under a given pressure. The extrusion molded
body of the explosive composition is cut at a length of 2.0 mm, which is dried to
obtain a composition shaped body for a columnar gas generating agent.
(Comparative Example 3)
[0061] In a rocking mixer are mixed 11 mass% of 5-aminotetrazole, 68 mass% of potassium
nitrate, 6 mass% of hydroxypropyl methylcellulose and 3 mass% of polyacrylamide, which
are mixed with 12 mass% of boron in a milling machine and further 15 parts by mass
of a deionized water is added per 100 parts by mass of the above component system
to conduct uniform milling. Then, the resulting milled mass is extruded into a predetermined
shape through a dice of 1.8 mm in diameter of an extruder under a given pressure.
The extrusion molded body of the explosive composition is cut at a length of 2.5 mm,
which is dried to obtain a composition shaped body for a columnar enhancer agent.
[0062] The extrusion moldability, fixation between shaped bodies, cleanability of a shaping
machine are observed with respect to the explosive composition shaped bodies for the
gas generating agent obtained in Examples 1 and 3, the composition shaped bodies for
the gas generating agent obtained in Comparative Examples 1 and 2, the explosive composition
shaped body for the enhancer agent obtained in Example 4 and the composition shaped
body for the enhancer agent obtained in Comparative Example 3 and further the explosive
composition shaped body for the gas generating agent obtained in Example 8. The results
are shown in Table 3. From these results, when the examples are compared with the
comparative examples, all of the examples are good in the extrusion moldability and
the cleanability of the shaping machine, and also the fixation between the shaped
bodies is not observed. On the contrary, the comparative examples are good in the
extrusion moldability, but the cleanability of the shaping machine is bad and the
fixation between the shaped bodies is observed. Moreover, each symbol in Table 3 means
the following.
[0063]
Extrusion moldability:
○ shaped by the extruder
X not shaped by the extruder
Cleanability of the shaping machine:
○ substances adhered to the extruder can be removed by hand
X substances adhered to the extruder can not be removed by hand, so that they can
be first removed by using a scraper after the substances adhered to each part are
made at a wet state with hot water.
[0064]
Table 3
| Example (comparative Example) |
Extrusion moldability |
Fixation between shaped bodies |
Cleanability of shaping machine |
| Example 1 |
○ |
none |
○ |
| Example 3 |
○ |
none |
○ |
| Example 4 |
○ |
none |
○ |
| Example 8 |
○ |
none |
○ |
| Comparative Example 1 |
○ |
presence |
X |
| Comparative Example 2 |
○ |
presence |
X |
| Comparative Example 3 |
○ |
presence |
X |
1. An explosive composition characterized by milling and drying a fuel component and an oxidizer component in the presence of
an aqueous emulsion of a hydrophobic tackifier.
2. The explosive composition according to claim 1, wherein a content of the hydrophobic
tackifier is 2-15 mass%.
3. The explosive composition according to claim 1 or 2, wherein the hydrophobic tackifier
is at least one selected from the group consisting of a rubber-based tackifier, an
acryl-based tackifier and a silicone-based tackifier.
4. The explosive composition according to claim 3, wherein the hydrophobic tackifier
is an acryl-based tackifier.
5. The explosive composition according to claim 3 or 4, wherein the hydrophobic tackifier
has a heat decomposition temperature of not lower than 200°C.
6. The explosive composition according to any one of claims 1-5, wherein the fuel component
is a nitrogen-containing compound and/or boron.
7. The explosive composition according to claim 6, wherein the nitrogen-containing compound
is at least one selected from the group consisting of guanidine, tetrazole, bitetrazole,
triazole, hydrazine, triazine, azodicarbonamide, dicyanamide and derivatives thereof
and a nitramine compound.
8. The explosive composition according to any one of claims 1-7, wherein the oxidizer
component is at least one selected from the group consisting of a chlorate, a perchlorate,
a nitrate and a basic nitrate.
9. The explosive composition according to claim 8, wherein the oxidizer component is
at least one selected from the group consisting of ammonium perchlorate, potassium
perchlorate, sodium perchlorate, potassium nitrate, sodium nitrate, strontium nitrate
and basic copper nitrate.
10. The explosive composition according to any one of claims 1-9, which further contains
at least one selected from a metallic powder, silicon nitride and a metal nitride.
11. The explosive composition according to any one of claims 1-10, which further contains
a surfactant.
12. The explosive composition according to claim 11, wherein the surfactant is a nonionic
surfactant having a HLB value of not more than 15.
13. An explosive composition shaped body characterized by milling, shaping and drying a fuel component and an oxidizer component as claimed
in any one of claims 1-9 in the presence of an aqueous emulsion of a hydrophobic tackifier.
14. The explosive composition shaped body according to claim 13, wherein the shaped body
is any of a gas generating agent, an autoignition agent and an enhancer agent.
15. The explosive composition shaped body according to claim 13 or 14, wherein the shaped
body is for an automotive safety device.
16. The explosive shaped body according to any one of claims 13-15, wherein the shaped
body has any of a granular form, a tablet form, a columnar form, a cylindrical form,
a prismatic form, a porous cylindrical form and a porous prismatic form.
17. The explosive composition shaped body according to any one of claims 13-16, which
further contains at least one selected from a metallic powder, silicon nitride and
a metal nitride.
18. The explosive composition shaped body according to any one of claims 13-17, which
further contains a surfactant.
19. The explosive composition shaped body according to claim 18, wherein the surfactant
is a nonionic surfactant having a HLB value of not more than 15.
20. A method of producing an explosive composition, which comprises milling a fuel component
and an oxidizer component with an aqueous emulsion of a hydrophobic tackifier and
drying them.
21. A method of producing an explosive composition shaped body, which comprises milling
a fuel component and an oxidizer component with an aqueous emulsion of a hydrophobic
tackifier and shaping, drying and solidifying them.
22. The method of producing an explosive composition shaped body according to claim 21,
wherein the shaping is an extrusion molding.