[0001] This invention relates to explosive compositions of matter and more particularly
it relates to slurry explosive compositions of matter.
[0002] Slurry explosives comprise inorganic oxidizing salt, fuel, a liquid solvent, disperser
or carrier for said salt and, optionally, at least one thickening agent. Although
the term "tslurry" is applied to such compositions the degree of consistency may range
from pourable or pumpable fluids of varying viscosity, through viscous extrudable
gels u
p to friable materials such as are described in Australian Patent Specification 483
568 and which may be packaged in the form of cartridges. The oxidizing salt component
usually comprises nitrate, chlorate or perchlorate of ammonia, sodium, potassium,
calcium or barium, the most extensively used salt being ammonium nitrate. The liquid
phase may vary widely in its chemical constitution, consistency, and explosive sensitivity.
Thus, in water- bearing slurries, the liquid phase may consist mainly of an aqueous
solution of inorganic oxidizing salt, but non-aqueous slurry compositions are known
wherein the liquid phase comprises a liquid chemical compound which acts as a fuel
to contribute energy to the composition. So as t6 increase the viscosity of slurry
explosives of the kind described thickening agents for example gums such as guar gum
or xanthan gums, or synthetic polymers such as polyacrylamide or copolymers thereof
have been used in an attempt to prevent segregation of the ingredients or to prevent
deterioration in wet conditions. It has also been proposed that improved homogeneity
and storage properties could be obtained by crosslinking the thickening agents with
crosslinking agents, for example potassium pyro- antimonate, sodium dichromate, potassium
dichromate or rare earth salts, or a redox system for example a mixture of an arsenious
compound and sodium dichromate. Whilst such attempts to modify the physical form and
storage properties of slurry explosives have been reasonably successful, it has been
observed that the rheology of these explosive compositions is somewhat dependent on
temperature. Thus for example when such compositions are stored or used in semi- tropical
or tropical areas it has been observed that the compositions became less coherent
and that certain of the components, such as metallic fuels, tended to segregate on
storage.
[0003] It has now been discovered that the addition of small amounts of fibrous material
to slurry explosive compositions of the type described improves the storage characteristics
of these compositions and modifies the rheological and physical properties of the
composition.
[0004] Accordingly there is provided a slurry explosive composition which comprises at least
one inorganic oxidizing salt, a liquid solvent disperser or carrier for said salt,
fuel material, optionally at least.one thickening agent which optionally may be crosslinked,
and as a rheology modifying agent an amount of fibrous material.
[0005] The fibrous material used in the invention should not be confused with the comminuted
or powdered irregularly shaped materials such as for example wood meal, sawdust, metallic
powders or flakes which have been used as fuel or sensitizing additives in prior art
explosive compositions. Our present fibrous material is distinct from such prior art
materials in that our fibrous materials are characterized in that they are derived
from materials in which the longitudinal/transverse dimensional ratio ranges from
about 10:1 to 1000:1 or more. By fibrous material we mean material which is formed
of fibres, the said fibres being thread-like bodies or filaments that at least in
part comprise, or can be derived from, animal or vegetable tissue, resinous materials,
polymeric materials or minerals. Natural fibre lengths vary from about 2 millimetres
for cellulose pulp fibres and asbestos fibres, up to 125 millimetres for wool, and
as much as 1000 millimetres for flax while many synthetic polymeric materials areavailable
in continuous filaments. Typical textile fibre diameters range from 0.01 to 0.04 microns
for asbestos fibrils which are the basis for the bunches or spicules of asbestos which
are commonly used to make asbestos-bearing products, whilst diameters of synthetic
fibres lie in range from 3 to 500 . microns. A diversity of fibrous materials is suitable
for use in the invention. Thus we have found that naturally occurring and synthetic
or man-made materials are useful, and within this wide class that inorganic or organic
materials are suitable. Examples of suitable materials include glass fibres, glass
rovings, anhydrite whiskers, ductile metal fibres, refractory oxide fibres such as
are available under the registered trade mark of "Saffil" and in the form of alumina
or zirconia; asbestos; carbon fibres; man-made fibres derived from cellulose such
as rayon, cellulose acetate or cellulose triacetate; fibres derived from synthetic
resins such as urea-formaldehyde, melamine-formaldehyde, or phenol-formaldehyde; polymeric
fibres used in the manufacture of textiles such as fibres of the acrylic type like
those fabricated from polyacrylonitrile, polyamides such as nylon 6 or nylon 66, polyesters
such as polyethylene terephthalate or polytetramethylene terephthalate, polyolefines
such as polyethylene, polypropylene or polytetrafluoroethylene, polyurethane fibres
such as those commonly referred to as spandex fibres, or fibres such as those from
the formal derivatives of poly- w vinyl alcohol. Vegetable fibres are also useful
and such materials are available in a range from fine threads to coarse fibres. Typically
useful vegetable fibres include hard vegetable fibres such as leaf fibres like sisal,
or. soft vegetable fibres of the bast type such as hemp or jute, or seed fibres like
kapok. Cotton fibresare also useful and fibres derived from animals such as wool or
cow- hair may also be used. If desired, mixtures of fibres may be used as a rheology
modifying agent. In instances where the fibrous material is derived from a polymer
such a polymer may be a homopolymer or a copolymer such as a block or graft copolymer
and may optionally he substituted or modified. It is convenient to use the fibres
in comparatively short lengths and many chopped fibres are available commercially
in lengths up to about 30 millimetres. Thus for example glass fibres used in the invention
are conveniently in the form of chopped rovings or strands having a length in a range
from about 3 to 12 millimetres. Such fibres often have a surface treatment comprising
a film forming material which reduces abrasion or fracture of the glass. Some fibres
like jute which has a fibre length in a range from l.to 5 millimetres or kapok which
has a fibre length in a range from 15 to 30 millimetres may not need to be converted
to shorter lengths prior to use, but other vegetable fibres such as sisal, which is
often in lengths from 600 to 1600 millimetres, or hemp ribbons which may be up to
5000 millimetres long will usually need to be shortened prior to use to lengths of
30 millimetres or less, typically in a range from 0.5 to 20 millimetres and often
in a range from 5 to 15 millimetres. Polymeric, resinous or man-made fibres may be
converted to any desired length prior to use and such lengths are similar to those
referred to above. The fibrous materials may have a circular or quasi- circular cross
section and dependent on their origin or mode of manufacture may be in the form of
solid rods or tubes. The diameter of such materials will vary, in the instances of
vegetable or animal fibres; thus jute fibres have a diameter in a range from about
14 to 20 microns whilst wool fibres have a diameter in a range from l8 to 40 microns
and sisal fibres range from about 125 to 500 microns in diameter. The diameter of
suitable synthetic fibres is more controllable than is the diameter of the naturally
occurring fibres and the use of synthetic fibres is preferred. A wide range of synthetic
fibres is available commercially from fine hosiery fibres to cords used for car tyre
manufacture. Typical suitable fibres are those having a diameter in a range from 5
to 100 microns, say in a range from 10 to 40 microns. The fibrous materials may also
be treated so as to be in a bulked form and synthetic fibres derived from rayon, polyacrylonitrile,
polyamides or polyesters are especially suitable for conversion to such a form. The
fibrous materials, especially those derived from synthetic polymers, may also contain
components derived from differing polymeric materials to provide heterogeneous or
conjugate fibres. They may also be fabricated so as to provide fibres in which the
cross-section is other than circular; thus the cross-section of a suitable fibre may
be for example tri-lobal. The amount of fibrous material used in the compositions
of the invention will depend to some extent on the nature of the fibre,. on the nature
of the composition to be modified and the extent to which it is desired to modify
the rheology of the composition. We have found that the incorporation of up to about
3% w/w, say from 0.001 to 2% w/w, of the composition of fibrous material is adequate
for most purposes and usually the amount of fibrous material used constitutes from
0.1 to 0.6% w/w of the composition.
[0006] In general, except for the rheology modifying agent, the compositions of our invention
are of conventional types. Thus the oxygen releasing salts used as ingredients in
our compositions may be, for example, inorganic nitrates, chlorates and perchlorates
and mixtures thereof. We prefer that the oxygen releasing salt material be chosen
from the perchlorates or nitrates of the alkali and alkaline earth metals or ammonium
and of these we prefer sodium nitrate, calcium nitrate, ammonium perchlorate and ammonium
nitrate. The amount of oxygen releasing salt in such compositions is not narrowly
critical; we have found that compositions containing amounts of oxygen releasing salts
from 30% w/w to 90% w/w of the total composition are satisfactory and amounts from
60% w/w to 85% w/w are preferred. The particle size and shape of the oxygen releasing
salt is not critical , .. , . r and is well known from the art of ammonium nitrate
manufacture; powders and prilled particles are satisfactory.
[0007] The liquid solvent, disperser or carrier for the oxygen releasing salt will, in the
more generally used compositions, be water but useful non-aqueous compositions can
be prepared wherein the liquid comprises non-aqueous liquids, for example diethylene
glycol, ethanolamine, formamide, dimethylformamide, dimethylsulphoxide, or liquid
salt mixtures comprising, for example, ammonium acetate or ammonium formate. When
water is used as the liquid the proportion thereof in the compositions should be sufficient
to dissolve at least part of the oxygen releasing inorganic salt and at least part
of any water soluble fuel which may be present, and also be sufficient to hydrate
at least part, preferably all, of any gummy gelling agent present. Suitably the amount
of water when present may constitute from 3% w/w to 35% w/w of the total composition,
but the amount present should not be in excess of the explosive limit of the composition.
We prefer that the water be in the range from 3% w/w to 25% w/w of the total composition.
In the instance where the explosive composition is of the pourable or pumpable type
it is more preferred that water constitute from 12% w/w to 17% w/w of the composition;
where the composition is of a friable type a very suitable range for the water content
is from 3% w/w to 14% w/w and a range from 4% w/w to 10% w/w is especially preferred.
When the said liquid is essent
" ially a non-aqueous liquid it suitably constitutes from 5 to 30% w/w of the composition.
A preferred class of non-aqueous liquids useful as components of the compositions
of the invention is the class of liquid amines as disclosed in the prior art explosive
compositions described in the specification of United States Patent 4,055,450. Such
liquid amines include alkylene diamines, alkanolamines and alkylamines and may be
typified by reference to amines such as ethylene diamine, ethanolamine, ethylamine,
diethylamine or butylamine. In the instance where the said liquid is in the form of
a melt derived from a mixture of salts it is convenient that the said liquid constitutes
from about 20 to about 60% w/w of the composition. Typically the liquid is derived
from a mixture of oxygen-releasing salt material such as ammonium nitrate, sodium
nitrate or calcium nitrate, and melt soluble fuel material such as carboxylates, thiocyanates,
amines or amides which may be typified by reference to substances such as ammonium
acetate, ammonium formate, ammonium thiocyanate, hexamethylene tetramine, dicyandiamidr,
thiourea, acetamide or urea. It is convenient that the fuel material component of
the said mixture of salts constitutes from about 30 to about 70% w/w of the said mixture
of salts. Such mixtures of salts are known and are described for example in the specification
of our copending Australian patent application 30130/77.
[0008] When referring to fuels or fuel materials in this specification we mean substances
which are stable in such explosive compositions, that is prior to detonation, during
preparation and storage the substance is chemically inert to the system. The said
substances must be combustible and their physical nature should be such that they
may be incorporated in our compositions in a manner so as to be uniformly distributed
throughout the compositions. Such fuels are well known in the art and they may be
organic or inorganic and may also be derived from animals and plants.
[0009] The fuels when employed in the compositions of this inventicn can be, for example,
non-explosive carbonaceous, non-metallic and metallic fuels or mixtures of the aforementioned
types of fuels. They can be varied widely.
[0010] Suitable fuels include organic water soluble substances for example urea, carbohydrates
such as sugars or molasses, water soluble alcohols or glycols, glues or mixtures of
these. Suitably the proportion of water soluble fuel in our compositions is in the
range from 0.5% w/w to 10% w/w, preferably from 4 to 7% w/w, of the total composition.
[0011] Other suitable fuels include water insolubleor sparingly water soluble materials
which may be chosen from inorganic materials for example sulphur, aluminium, silicon,
ferrosilicon, ferrophosphorus, magnesium, titanium, boron, mixtures thereof for example
mixtures of aluminium with ferrosilicon, or organic materials for example finely divided
charcoal, anthracite, gilsonite, asphalt, cellulosic materials such as sawdust, or
cereal products for example flours, dextrins or starches. When the inorganic fuel
is a metal it is preferably in granulated or powdered form. Such granulated or powdered
metal may be in the form of discrete particles, but metal powders wherein the metal
is in the form of flakes or in the form of aggregates of particles or flakes are also
satisfactory. Preferred fuels are the metallic powders. The most preferred metallic
fuel is aluminium. The proportion of water insoluble or sparingly water soluble non-metallic
fuels in such compositions may suitably be in the range from 1% w/w to 10% w/w of
the total composition and amounts from 4% w/w to 7% w/w of the total composition are
preferred. The proportion of metallic water insoluble fuels when present in such compositions
may be as high as 25% w/w and amounts in the range from 0.5% w/w to 20% w/w of the
total compositions are preferred.
[0012] Where desirable, it is convenient to add to the explosive compositions according
to our invention, in amounts expressed as parts by weight per 100 parts by weight
of the final mixture, other conventional additives used in slurry explosives. Such
additives may includefor example antifoaming agents, for example ethyl hexanol, in
amounts ranging e.g. from 0 to 0.1 part, or surfactants, for example non-ionic surfactants
such as alkylene oxide condensates of phenols, acids or amides, from 0 to 5 parts.
When desired, additional sensitisers in the form of gas or a mixture of gases such
as air may be added to our compositions. Thus it may be added in the form of injected
or stirred in air or gas or it may be added as air or gas encapsulated in or attached
to the surface of particulate material. Alternatively a gas, such as nitrogen or carbon
dioxide, may if desired be generated in the composition by known means, Where desirable
there may be included as a component of our compositions one or more conventional
thickening agents, for example gums such as the galactomannan or xanthan gums. Typical
examples of galactomannan gums are guar gum or derivatives thereof and locust bean
gum whilst the xanthan gums may be typified by reference to biopolymeric materials
which are produced by processes comprising the transformation of carbohydrate material
by means of micro-organisms such as those of the species of Xanthomonas. A very useful
biopolymeric material is that available under the trade name of "Biopolymer" XB23
which is derived from a polymer which has been reacted with Xanthomonas campestris.
Preferably such gums, when used in our compositions are in a crosslinked form. When
such gums are used in our compositions it is convenient to use amounts such that the
gum component comprises from 0.1 to 3% w/w, more usually from 0.3 to 1.5% w/w, of
the composition.
[0013] In general the explosive compositions of our invention may be prepared by the conventional
formulating techniques used for preparing slurry explosives. Thus for example a part
or all of the oxygen releasing salt may be in the form of a solution of the salt or
part may be incorporated in powdered or prilled form. Fuel materials when used may
also be incorporated in a dry form or alternatively in the form of a dispersion or
solution in part of the liquid component. It has been found convenient to add the
rheology modifying agent to the composition by adding the agent itself to the stirred
composition either at a constant rate of addition or in quanta or aliquots such that
the agent is dispersed through the composition. Alternatively a dispersion of the
modifying agent in a part of the liquid component may be added to and mixed with the
composition.
[0014] When guar gum is used as a component of the compositions of the invention it is preferred
that there be present in the composition a sufficiency of liquid to ensure that the
gum component is at least partially solvated. When agents are used to crosslink such
gum it is preferred that such an agent be added as one of the final ingredients. In
instances where such a crosslinking agent is a system comprising two or more components
it is desirable that whilst some of the components may be incorporated at any stage
of the preparation of the mixture, the last ingredient added is a component of the
crosslinking system. Thus for example when such a crosslinking system is a redox-system
it is desirable that the oxidizer component of that system be added to the composition
as the final ingredient. Other thickening agents such as synthetic polymers and copolymers
may also be used; for example polymers derived from acrylamide, and especially copolymers
derived from acrylamide and containing mer units which bear bidentate groups are satisfactory.
Typical examples of such copolymers are those derived from a major proportion of acrylamide
and a minor proportion of 2-acetoxyethyl methacrylate or methacryloyl- acetone optionally
with mer units derived from acrylonitrile.
[0015] The invention also includes a method of preparing a slurry explosive composition,
which method comprises mixing inorganic oxidizing salt and fuel material with a liquid
solvent disperser or carrier for said salt, optionally mixing therewith at least one
thickening agent which optionally may be crosslinked, to form a mixture and modifying
the rheology characteristics of said mixture by incorporating therein an amount of
fibrous material.
[0016] The compositions of the invention are advantageous over similar non-modified compositions
of the prior art in that the rheology of the compositions of the invention is such
that it provides enhanced resistance to physical change which may be induced by change
in temperature of the composition. The compositions of the invention are more robust
and coherent than are their unmodified counterparts of the prior art. Furthermore
the individual components of the composition do not tend to segregate as much as is
observed in unmodified similar prior art compositions.
[0017] The invention is now illustrated by, but is not limited to, the following examples
wherein all parts and percentages are expressed on a weight basis unless otherwise
specified. Examples 1, 11, 36 and 42 do not lie within the invention and are included
for the purposes of comparison.
Example 1
[0018] In this comparative example a water bearing explosive composition was prepared and
transferred to waxed paper containers to provide explosive cartridges. To an aqueous
solution containing 192 parts of water and 8 parts of a copolymer derived from acrylamide
and hydroxyethyl methacrylate in a molar percentage ratio of 95:5 there was added
16 parts of thiourea, 877 parts of powdered ammonium nitrate, 249 parts of sodium
nitrate and 116 parts of urea. The mixture was heated at a temperature of 40°C with
stirring to form a premix. To the premix so formed there was admixed 270 parts of
prilled ammonium nitrate, 140 parts of atomized aluminium powder the bulk of which
was capable of passing through a 200 mesh British Standard sieve and which was available
commercially under the designation of "Aluminium Powder 125" from Alcoa of Australia
Limited, and 60 parts of pregelled starch. When the resultant mixture was homogeneous
8 parts of a solution containing equal weights of water and sodium dichromate were
added and mixing was continued for 5 minutes. 18 parts of a solution containing equal
weights of water and sodium nitrite were then added followed by the admixture with
stirring of 60 parts of paint fine aluminium which was in the form of a powder the
bulk of which was capable of passing through a 325 mesh U.S. Bureau of Standards sieve
and which was available commercially from Alcoa of Australia Limited under thg. designation
of "Aluminium powder No 408". The resultant composition was pumped into waxed paper
containers to form explosive cartridges. The cartridges were detonable at a temperature
of 10°C using one No 8 aluminium detonator and had a velocity of detonation of 2.8
kilometres per second.
Examples 2 to 5 inclusive
[0019] The general procedure of Example 1 was repeated except that in the present examples
there was added, immediately prior to the incorporation of the sodium dichromate solution
into the composition, an amount of a fibrous component as set out below. In each example
it was observed that the resultant compositions were different in regard to their
rheological properties in comparison with the composition of Example 1. Shortly after
the fibrous material had been incorporated into the composition it was observed, in
general qualitative terms, that the compositions were more viscous and ultimately
assumed a coherent putty-like consistency. The compositions obtained were detonable.

Example 6
[0020] To 1490 parts of ethanolamine there was added 6177 parts of powdered ammonium nitrate
and 1990 parts of powdered sodium nitrate and the mixture was heated with stirring
to a temperature of 80°C. There was then added 50 parts of a surfactant which was
a condensate of stearic acid with ethylene oxide and contained 9 moles of ethylene
oxide per 1 mole of stearic acid, followed by 80 parts of hydroxypropyl guar gum.
The mixture was stirred until a weak gel began to form whereupon the stirred mixture
was cooled and 195 parts of nitrocellulose which was dampened with 30% of its weight
with water was incorporated into the stirred mixture, followed by 40 parts of bulked
polyacrylonitrile fibres which were from 15 to 25 millimetres in length. As the fibres
were incorporated into the stirred mixture, the composition changed from a weak gel
to a firm plastic composition. 15 parts of zinc chromate were then added to the composition
which was extruded into cylindrical cartridges which had been fabricated from waxed
paper. The cartridges were then detonated using two No 8 aluminium detonators.
Example 7
[0021] A dry premix was prepared by mixing 663 parts of powdered ammonium nitrate, 30 parts
of sodium nitrate, 100 parts of "Aluminium powder 125", and 6 parts of a xanthan gum
available under the designation "Biopolymer" XB23. To this premix there was added
50 parts of sugar dissolved in 110 parts of water. The resultant mixture was stirred
to a uniform mass during which time the gum became hydrated. A slurry of 40 parts
of water, 0.8 part of potassium antimony tartrate, 2.5 parts of asbestos fibres and
5 parts of chopped zirconia fibres was then added to and mixed with the mixture prepared
above and then 0.8 part of ceric sulphate was added. There was thus obtained a detonable,
strongly gelled explosive composition.
Example 8
[0022] 606 parts of powdered ammonium nitrate, 100 parts of sodium nitrate, 30 parts of
calcium nitrate, 20 parts of "Aluminium powder 125" and 4 parts of guar gum were blended
to form a mixture and to this mixture there was added with stirring a solution made
by dissolving 50 parts of sugar in 130 parts of water and in which there was dispersed
20 parts of gilsonite and 20 parts of sulphur. Stirring was continued until the guar
gum became hydrated and there was then added to the stirred mixture 3 parts of nylon
66 fibre and 20 parts of "Aluminium powder No 408". The resultant slurry explosive
was transferred to cylindrical cardboard tubes. They were stored for four weeks at
a temperature of 24°C and were detonable using 140 grams of pentolite.
Example 9
[0023] Using a mixer of the Schrader type having a capacity of 9 kilograms a mixture was
prepared by mixing 490 parts of prilled ammonium nitrate, 25 parts of powdered sodium
nitrate, 75 parts of sugar, 35Q parts of water and 10 parts of guar gum. To this mixture
was added 50 parts of reti- porous granules derived from melamine-formaldehyde resin
wherein the formaldehyde/melamine molar ratio was 4/1. Such granules act as agents
to sensitize explosive compositions to detonation and their preparation is discussed
in Example 12 of British Patent Specification 1,314,285. To this explosive composition
there was added a fibrous mixture containing 3 parts of nylon 6 fibre in which the
majority of the fibres were about 5 millimetres in length and 1 part of fibrous kapok.
The fibres were stirred into the mixture during which time the mixture was converted
from a pourable form to one which was viscous and putty-like. The composition so formed
was extruded into cardboard cylinders having a diameter of 12.5 centimetres and the
cartridges so formed were detonated using 300 grams of pentolite.
Example 10
[0024] A dispersion was prepared wherein 4 parts of guar gum were hydrated in a mixture
of 600 parts of ammonium nitrate, 130 parts of sodium nitrate, 136 parts of water,
50 parts of sugar, 30 parts of sulphur, 70 parts of aluminium, 20 parts of gilsonite
and 0.3 part of arsenious oxide. A fibrous slurry was prepared by dispersing 3 parts
of the nylon 66 fibres used in Example 2 in a solution which had been prepared by
dissolving 1 part of sodium dichromate in 9 parts of water. Using the apparatus described
in Examples l'and 3 of Belgian Patent Specification 778210 and the method of Example
4 of the same patent the dispersion was pumped at a rate of 32 kilograms per minute
through a loading hose to an attached interfacial surface generator mixer. The fibrous
slurry was pumped at a rate of 150 millilitres per minute and injected into the dispersion
just before the latter passed out of the loading hose and through the interfacial
surface generator mixer. The explosive composition so formed was thus located in a
borehole in the form of a stiff cohesive gel which was detonated successfully four
hours later.
Example 11
[0025] For the purposes of comparison a mixture was prepared from 3000 parts of ammonium
nitrate, 360 parts of thiourea, 5184 parts of water and 216 parts of the copolymer
used in Example 1 and there was then added with stirring 180 parts of a solution containing
equal weights of water and sodium dichromate. The mixture so prepared was placed in
polyethylene cylinders which had a diameter of 5 centimetres and a length of 5.5 centimetres,
and after 16 hours it was observed that the mixture had been converted to a gel. The
samples of the gel so obtained, which was a precursor of a slurry explosive composition,
were removed from the cylinders and were tested to destruction using the well known
testing device available under the registered trade mark of "Instron"and which is
used to determine the compression at the break point of materials. It was found that
the samples could be compressed by no more than 1.0 centimetre before they broke.
Examples 12 to 17 inclusive
[0026] The general procedure of Example 11 was repeated except that in each of Examples
12 to 17 there was added to the mixture immediately prior to the addition of the sodium
dichromate solution 150 parts of synthetic fibrous yarns as set out in Table 2. Table
2 also contains data relating to the yarn thickness and length, and the extent to
which the gels could be compressed prior to break. The products of these examples
were more robust than was the product of
comparative Example 11.

Examples 18 to 35 inclusive
[0027] In these examples a range of explosives compositions was prepared by the admixture
of differing fibrous materials in various amounts to a composition described in Example
1. The type, average length and average diameter of the fibrous materials, together
with the percentage which they constitute of the explosive composition is set out
in Table 3. in Table 3 also there is set down quantitative measurements of two stress
values which are related to the rigidity of the explosive composition; the greater
the stress value the more rigid is the composition. The stress values are related
to the magnitude of the forces required to deform a cylindrical sample of an explosive
composition either (a) along the longitudinal axis of the cylinder (axial stress)
or (b) at right angles to this longitudinal axis (lateral stress). The stress values,
which are referred to as axial and lateral stress gradients and defined hereinbelow,
are expressed as grams weight per cubic centimetre at a temperature of 19°C. The stress
values were determined by the following procedure: The "Instron" testing device referred
to in Example 11 was modified so that a cylindrical brass probe was secured to a crosshead
which was set to move downwrds at a constant rate of 1 centimetre per minute. To determine
the axial stress value a three day- old sample of the explosive composition was confined
in a cylindrical plastic vial of diameter 2.4 centimetres which fitted snugly into
a cylindrical hole in a jacketed sample holder maintained at a temperature of 19°C
by means of water circulated from a thermostated water-bath. The brass probe was lowered
so that it passed longitudinally through the sample, and the resistance of movement
of the probe through the sample as a function of the depth of penetration was detected
by conventional transducer means and recorded on conventional recording chart paper.
The stress value, referred to hereinbefore, is defined as the maximum value of the
gradient of a curve derived from values of the expression,

The lateral stress value was obtained in a similar manner except that the explosive
composition in the form of a cylinder of diameter of 2.5 centimetres was placed in
a groove in the sample holder and the probe was passed transversely through the sample.
In Table 3 the fibrous material referred to as "Spindrift" (Registered Trade Mark)
is a random polyester material containing a range of lengths and diameters of loose
and clumped fibres; and "Perlon" is a registered trade mark for material believed
to comprise polycaprolactam. The reference to "flock" materials is related to fibrous
materials available commercially in short, cut lengths and suitable for use as a raw
material in conventional electrostatic flocking processes.
Example 36
[0028] This is a comparative example wherein the composition of Example 1 was tested by
the procedures used in Examples 18 to 35 inclusive to determine the axial stress and
lateral stress values thereof. These are set out in Table 3 and it will be observed
that the values of this example are less than the corresponding values of Examples
18 to 35 inclusive.
Examples 37 to 41 inclusive
[0029] The general procedure of Examples 31 to 35 was repeated except that the axial and
lateral stress values were determined at a temperature of 38°C. The results obtained
are set out in Table 4.
Example 42
[0030] The general procedure of Example 36 was repeated except the axial and lateral stress
values were determined at a temperature of 38°C. The results obtained are set out
in Table 4 and it will be observed that the values of this comparative example are
less than the corresponding values of Examples 37 to 41 inclusive.

Example 43
[0031] 3490 parts of crushed ammonium nitrate, 1870 parts of urea and 640 parts of sodium
nitrate were placed in a container fitted with stirring means and heating means, and
the components were stirred and heated to a temperature of 70°C at which temperature
the components were in the form of a melt. To this melt there was added with stirring
20 parts of starch, 40 parts of ethylene glycol, 55 parts of fuel oil, 20 parts of
thiourea and 10 parts of a 50% aqeuous solution of sodium nitrite to form a mixture.
To the mixture so formed there added with stirring 3860 parts of prilled ammonium
nitrate to form a detonable explosive composition which was pumpable at ambient temperatures.
To this explosive composition there was incorporated 100 parts of flocked polyester
fibres which were 3-millimetres long. It was observed after the fibres had been added
to the composition that the viscosity of the composition increased.
1. A slurry explosive composition which comprises at least one inorganic oxidizing
salt, a liquid solvent disperser or carrier for said salt, fuel material, optionally
at least one thickening agent which optionally may be crosslinked, and as a rheology
modifying agent an amount which constitutes up to 3% w/w of the said composition of
fibrous material as hereinbefore defined.
2. A composition according to Claim 1 wherein the said fibrous material is derived
from material in which the ratio of the longitudinal dimension to the transverse dimension
is in a range from 10:1 to 1000:1.
3. A composition according to Claim 1 or Claim 2 wherein the said fibrous material
has a length in a range from 0.5 to 30 millimetres.
4. A composition according to any one of Claims 1 to 3 inclusive wherein the said
fibrous material is derived from a polymer selected from the group consisting of polyamides,
polyesters, polyolefines, polyurethanes and polyacrylonitriles.
5. A composition according to Claim 4 wherein the said fibrous material is selected
from the group consisting of nylon 6, nylon 66, poly(ethyleneterephthalate), poly-(ethylene)
and poly(acrylonitrile).
6. A composition according to any one of Claims 1 to 3 inclusive wherein the said
fibrous material is derived from material selected from the group consisting of asbestos,
glass and refractory oxides.
7. A composition according to Claim 6 wherein the said refractory oxide is selected
from the group consisting of alumina and zirconia.
8. A composition according to any one of Claims 1 to 3 inclusive wherein the said
fibrous material is derived from cellulose.
9. A composition according to any one of Claims 1 to 8 inclusive wherein the said
fibrous material constitutes from 0.001 to 2% w/w of the said composition.
10. A composition according to any one of Claims 1 to 8 inclusive wherein the said
fibrous material constitutes from 0.1 to 0.6% w/w of the said composition.
11. A composition according to any one of Claims 1 to 10 inclusive wherein the said
salt is selected from the group consisting of the perchlorates and nitrates of the
alkali metals, the alkaline earth metals and ammonium and constitutes from 30 to 90%
w/w of the said composition; the said liquid solvent, disperser or carrier constitutes
from 3 to 60% w/w of the said composition; the said fuel material is selected from
organic water soluble substances which constitute from 0.5 to 10% w/w of the said
composition, water insoluble and sparingly water soluble materials which constitute
from 1 to 10% w/w of the said composition, and metallic water insoluble materials
which constitute up to 25% w/w of the said composition; and the said thickening agent
is selected from the group.consisting of glactomannan gums, xanthan gums and polymeric
materials derived from acrylamide and constitutes from 0.1 to 3% w/w of the said composition.
12. A composition according to Claim 11 wherein the said salt is selected from the
group consisting of sodium nitrate, calcium nitrate and ammonium nitrate and constitutes
from 60 to 85% w/w of the said composition; the said liquid solvent is water and constitutes
from 3 to 25% of the said composition; the said fuel material is selected from organic
water soluble substances which constitute from 4 to 7% w/w of the said composition,
water insoluble and sparingly water soluble materials which constitute from 4 to 7%
w/w of the said composition, and metallic powders which constitute from 0.5 to 20%
w/w of the said composition; and the said thickening agent is selected from the group
consisting of guar gum, hydroxypropylguar gum, locust bean gum, biopolymeric material
derived from Xanthomonas campestris and copolymeric material containing a major proportion
of polyacrylamide and constitutes from 0.3 to 1.5% w/w of the said composition.
13. A process for the manufacture of a slurry explosive composition which process
comprises forming an explosive mixture comprising at least one inorganic oxidizing
salt, fuel material, optionally at least one thickening agent which optionally may
be crosslinked, and to said mixture adding up to 3% w/w of the said composition of
fibrous material as hereinbefore defined and incorporating said fibrous material into
said composition in a manner such that the rheological properties of the said composition
are modified.
14. A composition according to Claim 1 and substantially as described with reference
to any one of examples 2 to 10 inclusive and 18 to 35 inclusive and 43.
15. A process according to Claim 13 and substantially as described with reference
to any one of examples 2 to 10 inclusive and 18 to 35 inclusive and 43.