CA2301552C - Explosives gasser composition and method - Google Patents
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- C06—EXPLOSIVES; MATCHES
- C06B—EXPLOSIVES OR THERMIC COMPOSITIONS; MANUFACTURE THEREOF; USE OF SINGLE SUBSTANCES AS EXPLOSIVES
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Abstract
A gassing composition for gassing explosive compositions wherein, the gassing composition comprises a gassing agent and a metal salt having a divalent cation.
Description
EXPLOSIVES GASSER COMPOSITION AND METHOD
The present invention relates to improved chemical gassing of explosives, in particular to a gassing composition for use in explosives. The present invention also relates to a method of manufacturing explosives and to an explosive composition.
Civilian mining, quarrying and excavation industries commonly use bulk or packaged explosive formulations as a principal method for breaking rocks and ore for mining, building tunnels, excavating and similar activities.
Chemical gassing of explosive compositions, such as emulsion explosives, has been practised with chemical gassing agents such as sodium nitrite. These gassing agents may, in certain conditions take a considerable time to generate the desired gas and form a suitable gassed explosive. In commercial operations it is desirable to quickly generate the gas so that the explosive may be detonated. One of the problems associated with the gasser systems of the prior art is that the maximum gasser rate currently achievable is not sufficiently rapid for some applications. For example, this is a particular disadvantage when bulk explosives are loaded into large volume blastholes in cold climates because it may take several hours for the bulk explosive to fully gas. Attempts have been made to overcome this problem by keeping the emulsion temperature very high to maintain high gasser rates however the use of high emulsion temperatures can tend to cause the emulsion to breakdown during loading into a blasthole, particularly where the emulsion is pumped into the blasthole.
It is preferable that the gasser reaction commences shortly after the mixture of gasser composition and bulk emulsion is loaded into a blasthole and reaches completion rapidly.
Mining operations are usually carried out on a tight schedule and delays are minimised so that efficiency is maximised. Accordingly there are economic advantages to minimising the delay between the completion of loading and detonation of the blastholes. This is particularly important in underground blasting where an entire mine tunnel may have to be evacuated and activities in many areas halted while blasting is carried out. In many above ground and underground mines blasting is carried out at one set time each day and if the blastholes and explosives are not ready at the set time, then there is a 24 hour wait for the next opportunity to detonate the blastholes.
We have now found that improvements to the gassing of explosive compositions, including a far greater range of gassing rates and a higher maximum gassing rate, may be achieved by using one or more metal salts comprising divalent cations. Accordingly, the present invention provides a gassing composition for gassing an emulsion explosive composition wherein the gassing composition is in the form of a solution and comprises dissolved in the solution a gassing agent and a metal salt having a divalent cation, with the proviso that the metal salt is not iron sulphate, copper nitrate or iron nitrate.
The present invention further provides a method for gassing an emulsion explosive composition which comprises dispersing a gassing composition in accordance with the present invention into an explosive composition.
Additionally the present invention provides a gassed explosive composition comprising an emulsion explosive composition gassed by dispersing a gassing composition in accordance with the present invention into said emulsion explosive composition.
The invention also provides an emulsion explosive composition comprising an emulsifier and gas bubbles formed from a gassing composition in accordance with the present invention.
The invention further provides an emulsion explosive composition comprising an organic fuel as a continuous phase; an inorganic oxidizer salt solution or melt as a discontinuous phase; an emulsifier; and gas bubbles formed from a chemical gassing agent that is in the form of a solution and comprises dissolved in the solution a nitrite salt and divalent metal ion selected from the group consisting of calcium ion, strontium ion and mixtures thereof as a gassing enhancer.
The invention yet further provides a method for gassing an emulsion explosive = -3-composition comprising adding to a pre-formed emulsion phase a gassing composition in accordance with the present invention, and mixing the gassing agent uniformly throughout the emulsion phase to produce sensitizing gas bubbles.
The metal salt may be any convenient salt containing a divalent metal cation and includes simple salts, double salts, complexes and any other convenient means.
The divalent cation may be any divalent cation of a main group metal, transition metal, lanthanide or actinide. The divalent cation may preferably be formed from a main group metal of Group II, III, IV or V or a transition metal or mixtures thereof.
More preferably the divalent may be selected from the group consisting of Bee+, Mgt+' Cat+, Sr2+, Bat+, Tie+, Zr2+, Hf2+, V2+, CR2+, Mn2+, Fe 2+, Coe+, Nit+, Cue+, Zn2+, Age+, Hg2+, Cd2+, A12+, Sn2+, Pb2+
and mixtures thereof. In an embodiment, the divalent metal cation is selected from the group consisting of Mgt+, Cat+, Sr2+, Mn2+ and Zn2+. The most preferred divalent metal cations are Mg 2+ and Cat+.
The anion or anions, of the metal salt may be any suitable monovalent, divalent or trivalent anion. The metal salt may comprise more than one monovalent anion. The metal salt may be a double salt. Preferably the anion of the metal salt may be selected from the group consisting of halide, nitrate, sulphate, phosphate, chlorate, perchlorate and combinations thereof. More preferably the anion of the metal salt is nitrate. In one embodiment, the calcium ion is derived from calcium nitrate or a mixture including calcium nitrate. In another embodiment, the strontium ion is derived from strontium nitrate or a mixture including strontium nitrate. The yet another embodiment, the divalent metal ion comprises a strontium ion and the nitrite salt is added as an aqueous solution containing the ion.
The gassing composition is in the form of a solution. In use the solution is dispersed within the explosive. Typically the gassing composition comprises a chemical gassing agent and a divalent metal salt dissolved in a solvent or mixture of solvents.
The solvent may be any suitable liquid in which the chemical gasser agent and divalent metal salt are soluble, such as water. Advantageously, the gasser composition may be formed from separate solutions of gassing agent and metal salt, which solutions are blended immediately prior to their dispersal in the explosive.
The gassing agent is an agent suitable for the in situ chemical generation of gas bubbles and includes peroxides such as hydrogen peroxide, nitrite salts such as sodium nitrite and potassium nitrite, nitrosamines such as n, N'-dinitrosopentamethylenetetramine, diazonium ions/salts, alkali metal borohydrides such as sodium borohydride and bases such as carbonates including sodium carbonate.
Nitrite salts, and more preferably sodium nitrite, are preferred for use in the present invention. The nitrite salts react under conditions of acid pH to produce nitrogen gas bubbles.
Accelerators such as thiocyanate salts, iodides, sulphamic acid or its salts or thiourea may be used in the gassing composition to accelerate the gassing reaction.
Typically the gassing composition of the present invention may comprise gassing agent between 0.5 wt% and 45 wt% of the gassing composition and divalent metal salt between 1 wt% and 45 wt% of the gassing composition. Preferably the gassing composition comprises between 0.5 wt% and 25 wt% gassing agent and between 10 wt% and 40 wt%
divalent metal salt. More preferably the gasser composition comprises between 0.5 wt%
and 20 wt% gassing agent and between 20 wt% and 40 wt% divalent metal salt.
Optional accelerator, such as thiocyanate, may be present in the gassing composition at levels of between 0.05 wt% and 20 wt% of the gassing composition and preferably between 0.5 wt% and 10 wt%.
The gassing of the explosive compositions may preferably be carried out by forming a gassing composition by dissolving the gassing agent, the metal salt having a divalent cation and any optional additives in a solvent and dispersing the.gasser composition evenly throughout the explosive composition. The gassing composition subsequently reacts to generate gas bubbles in the explosive composition.
-4a-The gassing composition may be dispersed in the explosive composition at a level of between 0.5 and 10 wt% of the total composition or more typically between 0.5 wt% and 5 wt%.
The gassing composition of the present invention may be used in a wide variety of emulsion explosive compositions, including water-in-oil emulsions, oil-in-water emulsions (or slurries). Water-in-oil emulsions include, for example compositions where the emulsion is a water-in-oil emulsion, melt-in-fuel emulsion and melt-in-oil emulsion. The present invention will now be described in relation to water-in-oil emulsion explosives.
However those skilled in the art will readily understand that the gassing compositions may be used in other forms of explosive compositions with modifications adapted to account for the chemical interactions between the gasser composition and the explosive composition. When the explosive composition is a water-in-oil emulsion, typically the pH
of an aqueous phase of the water-in-oil emulsion is adjusted to 4.2 prior to dispersion of the gassing composition in the explosive composition.
It will be readily apparent to those skilled in the relevant technology however that certain divalent cation salts falling within the above description may have the desired effect on the gasser rate of an emulsion, but may be less preferred for use in a gasser solution or an emulsion explosives formulation. For example, the addition of FeSO4 to an emulsion explosive formulation comprising nitrate ions may cause production of large quantities of noxious fumes. Copper nitrate may also be an unsuitable additive in an emulsion explosive formulation due to the possibility of forming undesirable by-products, including a touch sensitive explosive such as copper tetramine nitrate. Some salts such as iron nitrate may be unsuitable if added to an emulsion explosive formulation in quantities which reduce pH or the gasser solution to an undesirable level.
The rate of gas formation by a gasser composition dispersed in an emulsion may be affected by a variety of parameters including the emulsion temperature, ambient temperature, ground temperature, the concentration of components in the gasser composition, the composition of the explosive composition and soforth.
Water-in-oil emulsion explosive compositions were first disclosed by Bluhm in United States Patent 3,447,978 and comprise (a) a discontinuous aqueous phase comprising discrete droplets of an aqueous solution of inorganic oxygen-releasing salts; (b) a continuous water-immiscible organic phase throughout which the droplets are dispersed and (c) an emulsifier which forms an emulsion of the droplets of oxidiser salt solution throughout the continuous organic phase.
Where these types of-emulsions comprise very little water or adventitious water only in the discontinuous phase they are more correctly referred to as melt-in-fuel emulsion explosives.
Preferably the emulsion suitable for use as an explosives emulsion is a water-in-oil or melt-in-oil emulsion or melt-in-fuel emulsion. Suitable oxygen releasing salts for use in the aqueous phase of the emulsion of the present invention include the alkali and alkaline earth metal nitrates, chlorates and perchlorates, ammonium nitrate, ammonium chlorate, ammonium perchlorate and mixtures thereof. The preferred oxygen releasing salts include ammonium nitrate, sodium nitrate and calcium nitrate. More preferably the oxygen releasing salt comprises ammonium nitrate or a mixture of ammonium nitrate and sodium or calcium nitrates.
Typically the oxygen releasing salt component of the compositions of the present invention comprise from 45 to 95 wt% and preferably from 60 to 90 wt% of the total emulsion composition. In compositions wherein the oxygen releasing salt comprises a mixture of ammonium nitrate and sodium nitrate or calcium nitrate the preferred composition range for such a blend is from 5 to 100 parts of sodium nitrate or calcium nitrate for every 100 parts of ammonium nitrate.
Typically the amount of water employed in the compositions of the present invention is in the range of from 0 (for a melt-in-fuel emulsion) to 30 wt% of the total emulsion composition.
Preferably the amount employed is from 4 to 25 wt% and more preferably from 6 to 25 wt%.
The continuous water immiscible organic phase of the emulsion composition of the present invention comprises the continuous "oil" phase of the emulsion composition and is the fuel.
Suitable organic fuels include aliphatic, alicyclic and aromatic compounds and mixtures thereof which are in the liquid state at the formulation temperature. Suitable organic fuels may be chosen from fuel oil, diesel oil, distillate, furnace oil, kerosene, naphtha, vegetable oils, waxes such as microcrystalline wax, paraffin wax and slack wax, paraffin oils, benzene, toluene, xylenes, asphaltic materials; polymeric oils such as the low molecular weight polymers of olefines, animal oils, fish oils and other mineral, hydrocarbon or fatty oils and mixtures thereof. Preferred organic fuels are liquid hydrocarbons generally referred to as petroleum distillates such as gasoline, kerosene, fuel oils and paraffin oils.
Typically the organic fuel or continuous phase of the emulsion comprises from 2 to 15 wt%
and preferably 3 to 10 wt% of the total composition.
In emulsion explosives, emulsifiers are used to decrease interfacial tension between the aqueous and oil phases. Molecules of the emulsifier locate at the interface between the aqueous droplet and continuous hydrocarbon phase. The emulsifier molecules are oriented with the hydrophilic head group in the aqueous droplet and the lipophilic tail in the continuous hydrocarbon phase. Emulsifiers stabilise the emulsion, inhibiting coalescence of the aqueous droplets and phase separation. Emulsifiers also inhibit crystallisation of oxidiser salt in the aqueous droplets which crystallisation can lead to emulsion breakdown and reduction in detonation sensitivity of the emulsion explosive composition.
The emulsifier of the emulsion composition of the present invention may comprise emulsifiers chosen from the wide range of emulsifiers known in the art for the preparation of emulsion explosive compositions. It is particularly preferred that the emulsifier used in the emulsion composition of the present invention is one of the well known emulsifiers based on the reaction products of poly[alk(en)yl] succinic anhydrides and alkylamines, including the polyisobutylene succinic anhydride (PiBSA)derivatives of alkanolamines.
Particularly preferred emulsifiers include condensation products of poly[alk(en)yl]
succinic anhydride with amines such as ethylene diamine, diethylene triamine and ethanolamine. Another preferred emulsifier for use in the emulsion composition of the present invention is a mixture of PiBSA
based and sodium mono-oleate based emulsifiers. Other suitable emulsifiers for use in the emulsion of the present invention include alcohol alkoxylates, phenol alkoxylates, poly(oxyalkylene)glycols, poly(oxyalkylene) fatty acid esters, amine alkoxylates, fatty acid esters of sorbitol and glycerol, fatty acid salts, sorbitan esters, poly(oxyalkylene) sorbitan esters, fatty amine alkoxylates, poly(oxyalkylene)glycol esters, fatty acid amines, fatty acid amide alkoxylates, fatty amines, quaternary amines, alkyloxazolines, alkenyloxazolines, imidazolines, alkylsulphonates, alkylarylsulphonates, alkylsulphosuccinates, alkylarylsulpnonates, alkylsulphosuccinates, alkylphosphates, alkenylphosphates, phosphate esters, lecithin, copolymers of poly(oxyalkylene)glycols and poly(12-hydroxystearic)acid and mixtures thereof.
Typically the emulsifier of the emulsion comprises up to 5 wt% of the emulsion. Higher proportions of the emulsifying agent may be used and may serve as supplemental fuel for the composition but in general it is not necessary to add more than 5 wt% of emulsifying agent to achieve the desired effect. Stable emulsions can be formed using relatively low levels of emulsifier and for reasons of economy it is preferable to keep the amount of emulsifying agent used at the minimum required to form the emulsion. The preferred level of emulsifying agent used is in the range of from 0.1 to 3.0 wt% of the water-in-oil emulsion.
If desired, other optional fuel materials, hereinafter referred to as secondary fuels may be incorporated into the emulsion in addition to the water immiscible organic fuel phase.
Examples of such secondary fuels include finely divided solids and water miscible organic liquids which can be used to partially replace water as a solvent for the oxygen releasing salts or to extend the aqueous solvent for the oxygen releasing salts. Examples of solid secondary fuels include finely divided materials such as sulphur, aluminium, urea and carbonaceous materials such as gilsonite, comminuted coke or charcoal, carbon black, resin acids such as .g_ abietic acid, sugars such as glucose or dextrose and vegetable products- such as starch, nut meal, grain meal and wood pulp. Examples of water miscible organic liquids include alcohols such as methanol, glycols such as ethylene glycol, amides such as formamide and urea and amines such as methylamine.
Typically the optional secondary fuel component of the composition of the present invention comprises from 0 to 30 wt% of the total composition.
Generally the emulsions themselves are not detonable and to form an explosive emulsion must be mixed with sensitising agents such as a self explosive (e.g.
trinitrotoluene or nitroglycerine) or a discontinuous phase of void agents. Sensitising using this explosives has been superseded by sensitisation methods which utilise nonexplosive sensitising agents. For example the incorporation of small voids into the emulsion which act as hot spots for propagating detonation may sensitize the emulsion and result in a detonable explosive.
The final density of the gassed emulsion may depend on the concentration of the components of the gasser composition but typically the final density is between 0.2 and 1.5 g/cc. Preferably the final density is between 0.5 and 1.3 g/cc or more preferably between 0.6 and 1.2 g/cc.
There may also be incorporated into the emulsion other substances or mixtures of substances which are oxygen releasing salts or which are themselves suitable as explosive materials. For example the emulsion may be mixed with prilled or particulate ammonium nitrate or ammonium nitrate/fuel oil mixtures to form so-called heavy ANFOs (or HANFOs).
The water-in-oil emulsion composition may be prepared by a number of different methods.
One preferred method of manufacture includes: dissolving said oxygen releasing salts in water at a temperature above the fudge point of the salt solution, preferably at a temperature in the range from 20 to 110 C to give an aqueous salt solution;
combining an aqueous salt solution, a water immiscible organic phase, and an emulsifier with rapid mixing to form a water-in-oil emulsion; and mixing until the emulsion is uniform.
Throughout this specification and the claims which follow, unless the context requires otherwise, the word "comprise", and variations such as "comprises" and "comprising", will be understood to imply the inclusion of a stated integer or step or group of integers or steps but not the exclusion of any other integer or step or group of integers or steps.
The invention is now demonstrated by but in no way limited to the following examples.
Example 1 In this example a number of different divalent salts were used in gasser compositions of the current invention which were added to portions of a water-in-oil emulsion.
The rate of gassing of each portion of emulsion was then measured.
- 9a-Preparation of a Water-in-Oil Emulsion A water-in-oil emulsion of the following composition was prepared for use in the example;
Oxidiser Solution -91 % w/w comprising ammonium nitrate (78.9 % w/w) water (20.7 % w/w) buffer (0.4 % w/w) Fuel Phase - 9 % w/w comprising a hydrocarbon oil/emulsifier mixture.
The emulsifier system comprised a mixture of a sorbitan mono-oleate derivative (SMO) and the uncondensed amide formed by the reaction of an alkanolamine with poly(isobutylene)succinic anhydride (PiBSA). The emulsion was prepared by dissolving ammonium nitrate in the water at elevated temperature (98 C) then adjusting the pH of the oxidiser solution so formed to 4.2. The fuel phase was then prepared by melting the microcrystalline wax and mixing it with the hydrocarbon oil/emulsifier system mixture. The oxidiser phase was then added in a slow stream to the fuel phase 98 C with rapid stirring to form a homogeneous water-in-oil emulsion.
The emulsion was then divided into numerous portions of equal mass.
Preparation of Gasser Compositions A series of gasser compositions were prepared by dissolving sodium nitrite and a divalent metal salt in water. All the gasser compositions comprised 5 wt% sodium nitrite and 35 wt%
divalent salt (with the exception of calcium chloride which was 32.5 wt% and magnesium sulphate which was 33.6 wt%). A control gasser composition was prepared by dissolving sodium nitrite (5 wt%) in water.
Addition of the Gasser Compositions to the Emulsion The water-in-oil emulsion was divided into numerous portion. Each of the gasser compositions was mixed into a separate portion of emulsion at 30 C, the gassing rate was measured and the relative rate constant at 30 C was calculated. The relative rate constant is the rate constant measured, divided by the rate constant for the control sample. The relative reaction rate constants for gasser compositions having different divalent metal salts are recorded in Table 1.
TABLE 1:
Metal Salt in Gasser Relative Rate Constant, k Control (no divalent metal salt) 1.0 Sodium nitrate (NaNO3) 0.9 Magnesium nitrate 4.4 (Mg(N03)2.6H2O
Calcium nitrate 4.1 (Ca(NO3)2.4H20) Strontium nitrate 1.8 (Sr(NO3)2) Manganese(II)nitrate 6.4 (Mn(N03)2.4H2O
Zinc nitrate 3.4 (Zn(N03)2. 6H20 Calcium chloride 2.7 (CaC12.6H20) Magnesium sulphate 1.6 (M SO .4H 0) The results in Table 1 show that the gasser compositions comprising divalent metal salts greatly increased the gasser rate compared to gasser compositions comprising monovalent metal salts or no metal salts. The presence of a divalent metal salt in a gasser composition appears to increase the gasser rate by up to six times. It is noted in particular that the gasser composition comprising the monovalent metal salt (sodium nitrate) and sodium nitrite gasses at a slower rate than the gasser composition which comprises sodium nitrite alone. It would appear therefore, that the presence of a monovalent metal salt may depress reaction rate.
Furthermore, for salts the catalytic effect decreases going down a column of the periodic table; for example magnesium nitrate has a greater effect per mole than calcium nitrate which in turn has a greater effect than strontium nitrate. Across a row of the periodic table, magnesium and zinc nitrate have a greater effect on gasser rate than calcium nitrate. These results tend to suggest that the increase in gassing rate appears to be approximately inversely proportional to the formula weight of the salt or the cation size.
Example 2 In this example a gasser composition of the present invention was added to a water-in-oil emulsion comprising a PiBSA based emulsifier system and compared with the results obtained in Example 1 where the gasser composition is added to an emulsion comprising a mixed PiBSA/SMO based emulsifier system.
Preparation of a Water-in-Oil Emulsion A water-in-oil emulsion was prepared as described is Example 1 but instead of a PiBSA/SMO
emulsifier system, PiBSA alone was used as emulsifier. Emulsion of this formulation was suitable for use in forming an explosives emulsion.
Preparation of Gasser Composition Two gasser compositions were prepared. The first gasser composition comprised 35 wt%
calcium nitrate and 5 wt% sodium nitrite in water. The second, control gasser composition comprised 5 wt% sodium nitrite in water.
Addition of the Gasser Compositions to the Emulsion The water-in-oil emulsion was divided into two portions. Each of the two gasser compositions were mixed into separate portions of emulsion at 30 C, the gasser rate was measured and the relative rate constant at 30 C was calculated. The relative rate constant is the rate constant measured, divided by the rate constant measured for the control sample. The reaction rate constants for two gasser compositions are recorded in Table 2.
TABLE 2:
Metal Salt in Gasser Relative Rate Constant, k Control (no divalent metal salt) 1 Calcium nitrate 2.5 (Ca(N03)2.4H20) The presence of the divalent metal salt (calcium nitrate) in the gasser composition increased the rate of gasser by 2.5 times the rate of gasser using the control gassing composition. It is noted that the gassing rate for the emulsion comprising PiBSA based emulsifier was less than the gassing rate for the equivalent emulsion comprising a mixed PiBSA/SMO
emulsifier system (Table 1).
Example 3 In this example the rate of reaction by gasser compositions of the current invention comprising a divalent metal salt and/or an accelerator were compared.
Preparation of a Water-in-Oil Emulsion A water-in-oil emulsion was prepared as described in Example 1.
Addition of the Gasser Compositions to the Emulsion A series of gasser compositions were prepared and added to separate portions of the water-in-oil emulsion. Each of the two gasser compositions were mixed into separate portions of emulsion at 30 C, the reaction rate was measured and the rate constant at 30 C was calculated. The relative rate constant is the rate constant measured, divided by the rate constant for the control sample. The relative reaction rate constants for two gasser compositions are recorded in Table 3.
TABLE 3:
Gasser Composition Relative Rate Constant, k Control - 5 wt% NaNO2, 1.0 no NaSCN, no divalent metal salt 5 wt% NaNO2 1.2 wt% NaSCN
5wt%NaNO, 4.1 10 35 wt% Ca(N03)2.4H,O
5 wt% NaNO2 10.0 10 wt% NaSCN
35 wt% Ca(N03)2.4H,O
It is noted that for each of the four samples, the final density of the gassed emulsion was 1.0 0.1 g/cc.
The results in Table 3 show that addition of thiocyanate alone to a solution of sodium nitrate gasser composition only marginally increases the reaction rate. Thiocyanate alone is a relatively poor gasser catalyst. However, when thiocyanate is added to a gasser composition comprising a divalent metal salt, there is a substantial increase in reaction rate; The reaction rate rises to around ten times the rate of gasser using the control and 2.5 times faster than using a divalent metal salt alone.
Example 4 The experiments described in Example 3 which were carried out at 30 C were repeated using emulsion and gasser composition at 5 C. The gassing rate for a gasser composition comprising divalent metal salt and thiocyanate was still 10 times the reaction rate using the control and 2.5 times faster than the reaction rate using a gasser composition comprising a divalent metal salt alone.
Exam le 5 The gassing times were also measured for the experiments described in Example 3 and the results are recorded in Table 4. The gassing time is the length of time taken for the gasser reaction to reach completion in an emulsion at 30 C.
TABLE 4:
Gasser Composition Gassing Time Control - 5 wt% NaNO2, no NaSCN, no 60 minutes divalent metal salt.
5 wt% NaNO2 52 minutes 10 wt% NaSCN
5 wt% NaNO2 17 minutes 35 wt% Ca(N03)2. 4H20 5 wt% NaNO2 8 minutes 10 wt% NaSCN
35 wt% Ca(NO) . 4H20 The results in Table 4 show that very fast gasser times can be obtained using the gassing composition of the present invention.
Example 6 Gasser compositions were made up using 5 wt% NaNO2 and a range of different concentrations of divalent cation salts. The gasser compositions were added to separate portions of emulsion made according to Example 1 and the gasser rate was measured. The reaction rates measured indicate that the extent of the increase in gasser rate is approximately proportional to the square of the nitrite salt concentration. Without wishing to be bound by theory it is believed that the divalent cation takes part twice in the rate limiting step of the gassing reaction mechanism.
Example 7 In this example gasser compositions of the present invention comprising different levels of divalent cation salt were added to a water-in-oil emulsion comprising a PiBSA/SMO based emulsifier system and the final gassed emulsion densities were measured.
Preparation of a Water-in-Oil Emulsion A water-in-oil emulsion was prepared as described in Example 1.
Preparation of Gasser Composition Gasser compositions of the following compositions were prepared:
TABLE 5:
Gasser Composition Emulsion Density, /cc Control - 5wt% NaNO2 0.98 no NaSCN, no divalent metal salt 5 wt % % NaNO, 0.97 10 wt% Mg(NO3).6H1O
5 wt% NaNO, 0.98 15 wt% Mg(NO3)2.6H20 5 wt% NaNO2 0.98 wt% Mg(NO3)2.6H20 Lw % NaNO2 0.97 t% M ( NO ),.6H,0 The results indicate that the level of divalent cation addition has negligible effect on the final emulsion density.
Example 8 The experiment described in Example 7 was repeated, the only difference being that all gasser compositions additionally included 10 wt% NaSCN. The densities measured for the gassed emulsions were all within the range 0.97-0.98 g/cc.
Accordingly, different levels of divalent cation salt in a gasser solution comprising sodium nitrite and sodium thiocyanate had no effect on the final density of the gassed emulsion.
Example 9 The samples of the emulsion of Example 1 at 26 C were mixed with 2.9wt% of gasser compositions of the following formulas;
Gasser Component Control Gasser Composition Gasser Composition Ti T2 NaNO2 (wt%) 15 15 15 NaSCN (wt%) 15 15 15 Ca(N03) 2 (wt%) 0 5 10 Water (wt%) 70 65 60 Gasser Compositions Ti and T2 comprise a divalent cation Ca2+ while the control gasser does not comprise a divalent cation.
The three samples of gasser composition mixed with emulsion were pumped into three separate vessels of equal volume at a loading rate of 70kg/minute.
The change in density versus time for each sample of gassed emulsion is depicted in Figure 1. Figure 1 illustrates a faster gasser rate and lower final density for the emulsion samples gassed with gasser compositions Ti and T2 than the control samples. Gasser composition T2, which comprises twice the content of divalent cation Ca compared to gasser composition Ti also exhibits the faster gasser rate.
While the invention has been explained in relation to its preferred embodiments it is to be understood that various modifications thereof will become apparent to those skilled in the art upon reading the specification. Therefore, it is to be understood that the invention disclosed herein is intended to cover such modifications as fall within the scope of the appended claims.
The present invention relates to improved chemical gassing of explosives, in particular to a gassing composition for use in explosives. The present invention also relates to a method of manufacturing explosives and to an explosive composition.
Civilian mining, quarrying and excavation industries commonly use bulk or packaged explosive formulations as a principal method for breaking rocks and ore for mining, building tunnels, excavating and similar activities.
Chemical gassing of explosive compositions, such as emulsion explosives, has been practised with chemical gassing agents such as sodium nitrite. These gassing agents may, in certain conditions take a considerable time to generate the desired gas and form a suitable gassed explosive. In commercial operations it is desirable to quickly generate the gas so that the explosive may be detonated. One of the problems associated with the gasser systems of the prior art is that the maximum gasser rate currently achievable is not sufficiently rapid for some applications. For example, this is a particular disadvantage when bulk explosives are loaded into large volume blastholes in cold climates because it may take several hours for the bulk explosive to fully gas. Attempts have been made to overcome this problem by keeping the emulsion temperature very high to maintain high gasser rates however the use of high emulsion temperatures can tend to cause the emulsion to breakdown during loading into a blasthole, particularly where the emulsion is pumped into the blasthole.
It is preferable that the gasser reaction commences shortly after the mixture of gasser composition and bulk emulsion is loaded into a blasthole and reaches completion rapidly.
Mining operations are usually carried out on a tight schedule and delays are minimised so that efficiency is maximised. Accordingly there are economic advantages to minimising the delay between the completion of loading and detonation of the blastholes. This is particularly important in underground blasting where an entire mine tunnel may have to be evacuated and activities in many areas halted while blasting is carried out. In many above ground and underground mines blasting is carried out at one set time each day and if the blastholes and explosives are not ready at the set time, then there is a 24 hour wait for the next opportunity to detonate the blastholes.
We have now found that improvements to the gassing of explosive compositions, including a far greater range of gassing rates and a higher maximum gassing rate, may be achieved by using one or more metal salts comprising divalent cations. Accordingly, the present invention provides a gassing composition for gassing an emulsion explosive composition wherein the gassing composition is in the form of a solution and comprises dissolved in the solution a gassing agent and a metal salt having a divalent cation, with the proviso that the metal salt is not iron sulphate, copper nitrate or iron nitrate.
The present invention further provides a method for gassing an emulsion explosive composition which comprises dispersing a gassing composition in accordance with the present invention into an explosive composition.
Additionally the present invention provides a gassed explosive composition comprising an emulsion explosive composition gassed by dispersing a gassing composition in accordance with the present invention into said emulsion explosive composition.
The invention also provides an emulsion explosive composition comprising an emulsifier and gas bubbles formed from a gassing composition in accordance with the present invention.
The invention further provides an emulsion explosive composition comprising an organic fuel as a continuous phase; an inorganic oxidizer salt solution or melt as a discontinuous phase; an emulsifier; and gas bubbles formed from a chemical gassing agent that is in the form of a solution and comprises dissolved in the solution a nitrite salt and divalent metal ion selected from the group consisting of calcium ion, strontium ion and mixtures thereof as a gassing enhancer.
The invention yet further provides a method for gassing an emulsion explosive = -3-composition comprising adding to a pre-formed emulsion phase a gassing composition in accordance with the present invention, and mixing the gassing agent uniformly throughout the emulsion phase to produce sensitizing gas bubbles.
The metal salt may be any convenient salt containing a divalent metal cation and includes simple salts, double salts, complexes and any other convenient means.
The divalent cation may be any divalent cation of a main group metal, transition metal, lanthanide or actinide. The divalent cation may preferably be formed from a main group metal of Group II, III, IV or V or a transition metal or mixtures thereof.
More preferably the divalent may be selected from the group consisting of Bee+, Mgt+' Cat+, Sr2+, Bat+, Tie+, Zr2+, Hf2+, V2+, CR2+, Mn2+, Fe 2+, Coe+, Nit+, Cue+, Zn2+, Age+, Hg2+, Cd2+, A12+, Sn2+, Pb2+
and mixtures thereof. In an embodiment, the divalent metal cation is selected from the group consisting of Mgt+, Cat+, Sr2+, Mn2+ and Zn2+. The most preferred divalent metal cations are Mg 2+ and Cat+.
The anion or anions, of the metal salt may be any suitable monovalent, divalent or trivalent anion. The metal salt may comprise more than one monovalent anion. The metal salt may be a double salt. Preferably the anion of the metal salt may be selected from the group consisting of halide, nitrate, sulphate, phosphate, chlorate, perchlorate and combinations thereof. More preferably the anion of the metal salt is nitrate. In one embodiment, the calcium ion is derived from calcium nitrate or a mixture including calcium nitrate. In another embodiment, the strontium ion is derived from strontium nitrate or a mixture including strontium nitrate. The yet another embodiment, the divalent metal ion comprises a strontium ion and the nitrite salt is added as an aqueous solution containing the ion.
The gassing composition is in the form of a solution. In use the solution is dispersed within the explosive. Typically the gassing composition comprises a chemical gassing agent and a divalent metal salt dissolved in a solvent or mixture of solvents.
The solvent may be any suitable liquid in which the chemical gasser agent and divalent metal salt are soluble, such as water. Advantageously, the gasser composition may be formed from separate solutions of gassing agent and metal salt, which solutions are blended immediately prior to their dispersal in the explosive.
The gassing agent is an agent suitable for the in situ chemical generation of gas bubbles and includes peroxides such as hydrogen peroxide, nitrite salts such as sodium nitrite and potassium nitrite, nitrosamines such as n, N'-dinitrosopentamethylenetetramine, diazonium ions/salts, alkali metal borohydrides such as sodium borohydride and bases such as carbonates including sodium carbonate.
Nitrite salts, and more preferably sodium nitrite, are preferred for use in the present invention. The nitrite salts react under conditions of acid pH to produce nitrogen gas bubbles.
Accelerators such as thiocyanate salts, iodides, sulphamic acid or its salts or thiourea may be used in the gassing composition to accelerate the gassing reaction.
Typically the gassing composition of the present invention may comprise gassing agent between 0.5 wt% and 45 wt% of the gassing composition and divalent metal salt between 1 wt% and 45 wt% of the gassing composition. Preferably the gassing composition comprises between 0.5 wt% and 25 wt% gassing agent and between 10 wt% and 40 wt%
divalent metal salt. More preferably the gasser composition comprises between 0.5 wt%
and 20 wt% gassing agent and between 20 wt% and 40 wt% divalent metal salt.
Optional accelerator, such as thiocyanate, may be present in the gassing composition at levels of between 0.05 wt% and 20 wt% of the gassing composition and preferably between 0.5 wt% and 10 wt%.
The gassing of the explosive compositions may preferably be carried out by forming a gassing composition by dissolving the gassing agent, the metal salt having a divalent cation and any optional additives in a solvent and dispersing the.gasser composition evenly throughout the explosive composition. The gassing composition subsequently reacts to generate gas bubbles in the explosive composition.
-4a-The gassing composition may be dispersed in the explosive composition at a level of between 0.5 and 10 wt% of the total composition or more typically between 0.5 wt% and 5 wt%.
The gassing composition of the present invention may be used in a wide variety of emulsion explosive compositions, including water-in-oil emulsions, oil-in-water emulsions (or slurries). Water-in-oil emulsions include, for example compositions where the emulsion is a water-in-oil emulsion, melt-in-fuel emulsion and melt-in-oil emulsion. The present invention will now be described in relation to water-in-oil emulsion explosives.
However those skilled in the art will readily understand that the gassing compositions may be used in other forms of explosive compositions with modifications adapted to account for the chemical interactions between the gasser composition and the explosive composition. When the explosive composition is a water-in-oil emulsion, typically the pH
of an aqueous phase of the water-in-oil emulsion is adjusted to 4.2 prior to dispersion of the gassing composition in the explosive composition.
It will be readily apparent to those skilled in the relevant technology however that certain divalent cation salts falling within the above description may have the desired effect on the gasser rate of an emulsion, but may be less preferred for use in a gasser solution or an emulsion explosives formulation. For example, the addition of FeSO4 to an emulsion explosive formulation comprising nitrate ions may cause production of large quantities of noxious fumes. Copper nitrate may also be an unsuitable additive in an emulsion explosive formulation due to the possibility of forming undesirable by-products, including a touch sensitive explosive such as copper tetramine nitrate. Some salts such as iron nitrate may be unsuitable if added to an emulsion explosive formulation in quantities which reduce pH or the gasser solution to an undesirable level.
The rate of gas formation by a gasser composition dispersed in an emulsion may be affected by a variety of parameters including the emulsion temperature, ambient temperature, ground temperature, the concentration of components in the gasser composition, the composition of the explosive composition and soforth.
Water-in-oil emulsion explosive compositions were first disclosed by Bluhm in United States Patent 3,447,978 and comprise (a) a discontinuous aqueous phase comprising discrete droplets of an aqueous solution of inorganic oxygen-releasing salts; (b) a continuous water-immiscible organic phase throughout which the droplets are dispersed and (c) an emulsifier which forms an emulsion of the droplets of oxidiser salt solution throughout the continuous organic phase.
Where these types of-emulsions comprise very little water or adventitious water only in the discontinuous phase they are more correctly referred to as melt-in-fuel emulsion explosives.
Preferably the emulsion suitable for use as an explosives emulsion is a water-in-oil or melt-in-oil emulsion or melt-in-fuel emulsion. Suitable oxygen releasing salts for use in the aqueous phase of the emulsion of the present invention include the alkali and alkaline earth metal nitrates, chlorates and perchlorates, ammonium nitrate, ammonium chlorate, ammonium perchlorate and mixtures thereof. The preferred oxygen releasing salts include ammonium nitrate, sodium nitrate and calcium nitrate. More preferably the oxygen releasing salt comprises ammonium nitrate or a mixture of ammonium nitrate and sodium or calcium nitrates.
Typically the oxygen releasing salt component of the compositions of the present invention comprise from 45 to 95 wt% and preferably from 60 to 90 wt% of the total emulsion composition. In compositions wherein the oxygen releasing salt comprises a mixture of ammonium nitrate and sodium nitrate or calcium nitrate the preferred composition range for such a blend is from 5 to 100 parts of sodium nitrate or calcium nitrate for every 100 parts of ammonium nitrate.
Typically the amount of water employed in the compositions of the present invention is in the range of from 0 (for a melt-in-fuel emulsion) to 30 wt% of the total emulsion composition.
Preferably the amount employed is from 4 to 25 wt% and more preferably from 6 to 25 wt%.
The continuous water immiscible organic phase of the emulsion composition of the present invention comprises the continuous "oil" phase of the emulsion composition and is the fuel.
Suitable organic fuels include aliphatic, alicyclic and aromatic compounds and mixtures thereof which are in the liquid state at the formulation temperature. Suitable organic fuels may be chosen from fuel oil, diesel oil, distillate, furnace oil, kerosene, naphtha, vegetable oils, waxes such as microcrystalline wax, paraffin wax and slack wax, paraffin oils, benzene, toluene, xylenes, asphaltic materials; polymeric oils such as the low molecular weight polymers of olefines, animal oils, fish oils and other mineral, hydrocarbon or fatty oils and mixtures thereof. Preferred organic fuels are liquid hydrocarbons generally referred to as petroleum distillates such as gasoline, kerosene, fuel oils and paraffin oils.
Typically the organic fuel or continuous phase of the emulsion comprises from 2 to 15 wt%
and preferably 3 to 10 wt% of the total composition.
In emulsion explosives, emulsifiers are used to decrease interfacial tension between the aqueous and oil phases. Molecules of the emulsifier locate at the interface between the aqueous droplet and continuous hydrocarbon phase. The emulsifier molecules are oriented with the hydrophilic head group in the aqueous droplet and the lipophilic tail in the continuous hydrocarbon phase. Emulsifiers stabilise the emulsion, inhibiting coalescence of the aqueous droplets and phase separation. Emulsifiers also inhibit crystallisation of oxidiser salt in the aqueous droplets which crystallisation can lead to emulsion breakdown and reduction in detonation sensitivity of the emulsion explosive composition.
The emulsifier of the emulsion composition of the present invention may comprise emulsifiers chosen from the wide range of emulsifiers known in the art for the preparation of emulsion explosive compositions. It is particularly preferred that the emulsifier used in the emulsion composition of the present invention is one of the well known emulsifiers based on the reaction products of poly[alk(en)yl] succinic anhydrides and alkylamines, including the polyisobutylene succinic anhydride (PiBSA)derivatives of alkanolamines.
Particularly preferred emulsifiers include condensation products of poly[alk(en)yl]
succinic anhydride with amines such as ethylene diamine, diethylene triamine and ethanolamine. Another preferred emulsifier for use in the emulsion composition of the present invention is a mixture of PiBSA
based and sodium mono-oleate based emulsifiers. Other suitable emulsifiers for use in the emulsion of the present invention include alcohol alkoxylates, phenol alkoxylates, poly(oxyalkylene)glycols, poly(oxyalkylene) fatty acid esters, amine alkoxylates, fatty acid esters of sorbitol and glycerol, fatty acid salts, sorbitan esters, poly(oxyalkylene) sorbitan esters, fatty amine alkoxylates, poly(oxyalkylene)glycol esters, fatty acid amines, fatty acid amide alkoxylates, fatty amines, quaternary amines, alkyloxazolines, alkenyloxazolines, imidazolines, alkylsulphonates, alkylarylsulphonates, alkylsulphosuccinates, alkylarylsulpnonates, alkylsulphosuccinates, alkylphosphates, alkenylphosphates, phosphate esters, lecithin, copolymers of poly(oxyalkylene)glycols and poly(12-hydroxystearic)acid and mixtures thereof.
Typically the emulsifier of the emulsion comprises up to 5 wt% of the emulsion. Higher proportions of the emulsifying agent may be used and may serve as supplemental fuel for the composition but in general it is not necessary to add more than 5 wt% of emulsifying agent to achieve the desired effect. Stable emulsions can be formed using relatively low levels of emulsifier and for reasons of economy it is preferable to keep the amount of emulsifying agent used at the minimum required to form the emulsion. The preferred level of emulsifying agent used is in the range of from 0.1 to 3.0 wt% of the water-in-oil emulsion.
If desired, other optional fuel materials, hereinafter referred to as secondary fuels may be incorporated into the emulsion in addition to the water immiscible organic fuel phase.
Examples of such secondary fuels include finely divided solids and water miscible organic liquids which can be used to partially replace water as a solvent for the oxygen releasing salts or to extend the aqueous solvent for the oxygen releasing salts. Examples of solid secondary fuels include finely divided materials such as sulphur, aluminium, urea and carbonaceous materials such as gilsonite, comminuted coke or charcoal, carbon black, resin acids such as .g_ abietic acid, sugars such as glucose or dextrose and vegetable products- such as starch, nut meal, grain meal and wood pulp. Examples of water miscible organic liquids include alcohols such as methanol, glycols such as ethylene glycol, amides such as formamide and urea and amines such as methylamine.
Typically the optional secondary fuel component of the composition of the present invention comprises from 0 to 30 wt% of the total composition.
Generally the emulsions themselves are not detonable and to form an explosive emulsion must be mixed with sensitising agents such as a self explosive (e.g.
trinitrotoluene or nitroglycerine) or a discontinuous phase of void agents. Sensitising using this explosives has been superseded by sensitisation methods which utilise nonexplosive sensitising agents. For example the incorporation of small voids into the emulsion which act as hot spots for propagating detonation may sensitize the emulsion and result in a detonable explosive.
The final density of the gassed emulsion may depend on the concentration of the components of the gasser composition but typically the final density is between 0.2 and 1.5 g/cc. Preferably the final density is between 0.5 and 1.3 g/cc or more preferably between 0.6 and 1.2 g/cc.
There may also be incorporated into the emulsion other substances or mixtures of substances which are oxygen releasing salts or which are themselves suitable as explosive materials. For example the emulsion may be mixed with prilled or particulate ammonium nitrate or ammonium nitrate/fuel oil mixtures to form so-called heavy ANFOs (or HANFOs).
The water-in-oil emulsion composition may be prepared by a number of different methods.
One preferred method of manufacture includes: dissolving said oxygen releasing salts in water at a temperature above the fudge point of the salt solution, preferably at a temperature in the range from 20 to 110 C to give an aqueous salt solution;
combining an aqueous salt solution, a water immiscible organic phase, and an emulsifier with rapid mixing to form a water-in-oil emulsion; and mixing until the emulsion is uniform.
Throughout this specification and the claims which follow, unless the context requires otherwise, the word "comprise", and variations such as "comprises" and "comprising", will be understood to imply the inclusion of a stated integer or step or group of integers or steps but not the exclusion of any other integer or step or group of integers or steps.
The invention is now demonstrated by but in no way limited to the following examples.
Example 1 In this example a number of different divalent salts were used in gasser compositions of the current invention which were added to portions of a water-in-oil emulsion.
The rate of gassing of each portion of emulsion was then measured.
- 9a-Preparation of a Water-in-Oil Emulsion A water-in-oil emulsion of the following composition was prepared for use in the example;
Oxidiser Solution -91 % w/w comprising ammonium nitrate (78.9 % w/w) water (20.7 % w/w) buffer (0.4 % w/w) Fuel Phase - 9 % w/w comprising a hydrocarbon oil/emulsifier mixture.
The emulsifier system comprised a mixture of a sorbitan mono-oleate derivative (SMO) and the uncondensed amide formed by the reaction of an alkanolamine with poly(isobutylene)succinic anhydride (PiBSA). The emulsion was prepared by dissolving ammonium nitrate in the water at elevated temperature (98 C) then adjusting the pH of the oxidiser solution so formed to 4.2. The fuel phase was then prepared by melting the microcrystalline wax and mixing it with the hydrocarbon oil/emulsifier system mixture. The oxidiser phase was then added in a slow stream to the fuel phase 98 C with rapid stirring to form a homogeneous water-in-oil emulsion.
The emulsion was then divided into numerous portions of equal mass.
Preparation of Gasser Compositions A series of gasser compositions were prepared by dissolving sodium nitrite and a divalent metal salt in water. All the gasser compositions comprised 5 wt% sodium nitrite and 35 wt%
divalent salt (with the exception of calcium chloride which was 32.5 wt% and magnesium sulphate which was 33.6 wt%). A control gasser composition was prepared by dissolving sodium nitrite (5 wt%) in water.
Addition of the Gasser Compositions to the Emulsion The water-in-oil emulsion was divided into numerous portion. Each of the gasser compositions was mixed into a separate portion of emulsion at 30 C, the gassing rate was measured and the relative rate constant at 30 C was calculated. The relative rate constant is the rate constant measured, divided by the rate constant for the control sample. The relative reaction rate constants for gasser compositions having different divalent metal salts are recorded in Table 1.
TABLE 1:
Metal Salt in Gasser Relative Rate Constant, k Control (no divalent metal salt) 1.0 Sodium nitrate (NaNO3) 0.9 Magnesium nitrate 4.4 (Mg(N03)2.6H2O
Calcium nitrate 4.1 (Ca(NO3)2.4H20) Strontium nitrate 1.8 (Sr(NO3)2) Manganese(II)nitrate 6.4 (Mn(N03)2.4H2O
Zinc nitrate 3.4 (Zn(N03)2. 6H20 Calcium chloride 2.7 (CaC12.6H20) Magnesium sulphate 1.6 (M SO .4H 0) The results in Table 1 show that the gasser compositions comprising divalent metal salts greatly increased the gasser rate compared to gasser compositions comprising monovalent metal salts or no metal salts. The presence of a divalent metal salt in a gasser composition appears to increase the gasser rate by up to six times. It is noted in particular that the gasser composition comprising the monovalent metal salt (sodium nitrate) and sodium nitrite gasses at a slower rate than the gasser composition which comprises sodium nitrite alone. It would appear therefore, that the presence of a monovalent metal salt may depress reaction rate.
Furthermore, for salts the catalytic effect decreases going down a column of the periodic table; for example magnesium nitrate has a greater effect per mole than calcium nitrate which in turn has a greater effect than strontium nitrate. Across a row of the periodic table, magnesium and zinc nitrate have a greater effect on gasser rate than calcium nitrate. These results tend to suggest that the increase in gassing rate appears to be approximately inversely proportional to the formula weight of the salt or the cation size.
Example 2 In this example a gasser composition of the present invention was added to a water-in-oil emulsion comprising a PiBSA based emulsifier system and compared with the results obtained in Example 1 where the gasser composition is added to an emulsion comprising a mixed PiBSA/SMO based emulsifier system.
Preparation of a Water-in-Oil Emulsion A water-in-oil emulsion was prepared as described is Example 1 but instead of a PiBSA/SMO
emulsifier system, PiBSA alone was used as emulsifier. Emulsion of this formulation was suitable for use in forming an explosives emulsion.
Preparation of Gasser Composition Two gasser compositions were prepared. The first gasser composition comprised 35 wt%
calcium nitrate and 5 wt% sodium nitrite in water. The second, control gasser composition comprised 5 wt% sodium nitrite in water.
Addition of the Gasser Compositions to the Emulsion The water-in-oil emulsion was divided into two portions. Each of the two gasser compositions were mixed into separate portions of emulsion at 30 C, the gasser rate was measured and the relative rate constant at 30 C was calculated. The relative rate constant is the rate constant measured, divided by the rate constant measured for the control sample. The reaction rate constants for two gasser compositions are recorded in Table 2.
TABLE 2:
Metal Salt in Gasser Relative Rate Constant, k Control (no divalent metal salt) 1 Calcium nitrate 2.5 (Ca(N03)2.4H20) The presence of the divalent metal salt (calcium nitrate) in the gasser composition increased the rate of gasser by 2.5 times the rate of gasser using the control gassing composition. It is noted that the gassing rate for the emulsion comprising PiBSA based emulsifier was less than the gassing rate for the equivalent emulsion comprising a mixed PiBSA/SMO
emulsifier system (Table 1).
Example 3 In this example the rate of reaction by gasser compositions of the current invention comprising a divalent metal salt and/or an accelerator were compared.
Preparation of a Water-in-Oil Emulsion A water-in-oil emulsion was prepared as described in Example 1.
Addition of the Gasser Compositions to the Emulsion A series of gasser compositions were prepared and added to separate portions of the water-in-oil emulsion. Each of the two gasser compositions were mixed into separate portions of emulsion at 30 C, the reaction rate was measured and the rate constant at 30 C was calculated. The relative rate constant is the rate constant measured, divided by the rate constant for the control sample. The relative reaction rate constants for two gasser compositions are recorded in Table 3.
TABLE 3:
Gasser Composition Relative Rate Constant, k Control - 5 wt% NaNO2, 1.0 no NaSCN, no divalent metal salt 5 wt% NaNO2 1.2 wt% NaSCN
5wt%NaNO, 4.1 10 35 wt% Ca(N03)2.4H,O
5 wt% NaNO2 10.0 10 wt% NaSCN
35 wt% Ca(N03)2.4H,O
It is noted that for each of the four samples, the final density of the gassed emulsion was 1.0 0.1 g/cc.
The results in Table 3 show that addition of thiocyanate alone to a solution of sodium nitrate gasser composition only marginally increases the reaction rate. Thiocyanate alone is a relatively poor gasser catalyst. However, when thiocyanate is added to a gasser composition comprising a divalent metal salt, there is a substantial increase in reaction rate; The reaction rate rises to around ten times the rate of gasser using the control and 2.5 times faster than using a divalent metal salt alone.
Example 4 The experiments described in Example 3 which were carried out at 30 C were repeated using emulsion and gasser composition at 5 C. The gassing rate for a gasser composition comprising divalent metal salt and thiocyanate was still 10 times the reaction rate using the control and 2.5 times faster than the reaction rate using a gasser composition comprising a divalent metal salt alone.
Exam le 5 The gassing times were also measured for the experiments described in Example 3 and the results are recorded in Table 4. The gassing time is the length of time taken for the gasser reaction to reach completion in an emulsion at 30 C.
TABLE 4:
Gasser Composition Gassing Time Control - 5 wt% NaNO2, no NaSCN, no 60 minutes divalent metal salt.
5 wt% NaNO2 52 minutes 10 wt% NaSCN
5 wt% NaNO2 17 minutes 35 wt% Ca(N03)2. 4H20 5 wt% NaNO2 8 minutes 10 wt% NaSCN
35 wt% Ca(NO) . 4H20 The results in Table 4 show that very fast gasser times can be obtained using the gassing composition of the present invention.
Example 6 Gasser compositions were made up using 5 wt% NaNO2 and a range of different concentrations of divalent cation salts. The gasser compositions were added to separate portions of emulsion made according to Example 1 and the gasser rate was measured. The reaction rates measured indicate that the extent of the increase in gasser rate is approximately proportional to the square of the nitrite salt concentration. Without wishing to be bound by theory it is believed that the divalent cation takes part twice in the rate limiting step of the gassing reaction mechanism.
Example 7 In this example gasser compositions of the present invention comprising different levels of divalent cation salt were added to a water-in-oil emulsion comprising a PiBSA/SMO based emulsifier system and the final gassed emulsion densities were measured.
Preparation of a Water-in-Oil Emulsion A water-in-oil emulsion was prepared as described in Example 1.
Preparation of Gasser Composition Gasser compositions of the following compositions were prepared:
TABLE 5:
Gasser Composition Emulsion Density, /cc Control - 5wt% NaNO2 0.98 no NaSCN, no divalent metal salt 5 wt % % NaNO, 0.97 10 wt% Mg(NO3).6H1O
5 wt% NaNO, 0.98 15 wt% Mg(NO3)2.6H20 5 wt% NaNO2 0.98 wt% Mg(NO3)2.6H20 Lw % NaNO2 0.97 t% M ( NO ),.6H,0 The results indicate that the level of divalent cation addition has negligible effect on the final emulsion density.
Example 8 The experiment described in Example 7 was repeated, the only difference being that all gasser compositions additionally included 10 wt% NaSCN. The densities measured for the gassed emulsions were all within the range 0.97-0.98 g/cc.
Accordingly, different levels of divalent cation salt in a gasser solution comprising sodium nitrite and sodium thiocyanate had no effect on the final density of the gassed emulsion.
Example 9 The samples of the emulsion of Example 1 at 26 C were mixed with 2.9wt% of gasser compositions of the following formulas;
Gasser Component Control Gasser Composition Gasser Composition Ti T2 NaNO2 (wt%) 15 15 15 NaSCN (wt%) 15 15 15 Ca(N03) 2 (wt%) 0 5 10 Water (wt%) 70 65 60 Gasser Compositions Ti and T2 comprise a divalent cation Ca2+ while the control gasser does not comprise a divalent cation.
The three samples of gasser composition mixed with emulsion were pumped into three separate vessels of equal volume at a loading rate of 70kg/minute.
The change in density versus time for each sample of gassed emulsion is depicted in Figure 1. Figure 1 illustrates a faster gasser rate and lower final density for the emulsion samples gassed with gasser compositions Ti and T2 than the control samples. Gasser composition T2, which comprises twice the content of divalent cation Ca compared to gasser composition Ti also exhibits the faster gasser rate.
While the invention has been explained in relation to its preferred embodiments it is to be understood that various modifications thereof will become apparent to those skilled in the art upon reading the specification. Therefore, it is to be understood that the invention disclosed herein is intended to cover such modifications as fall within the scope of the appended claims.
Claims (42)
1. A gassing composition for gassing an emulsion explosive composition wherein the gassing composition is in the form of a solution and comprises dissolved in the solution a gassing agent and a metal salt having a divalent cation, with the proviso that the metal salt is not iron sulphate, copper nitrate or iron nitrate.
2. A gassing composition according to claim 1 wherein the cation is selected from the group consisting of any divalent cation of a main group metal, transition metal, lanthanide or actinide.
3. A gassing composition according to claim 1 wherein the divalent is selected from the group consisting of Be2+, Mg2+, Ca2+,Sr2+, Ba2+, Ti2+, Zr2+, Hf2+, V2+, Cr2+, Mn2+, Fe2+, Co2+, Ni2+, Cu2+, Zn2+, Ag2+, Hg2+, Cd2+, Al2+, Sn2+, Pb2+, and mixtures thereof.
4. A gassing composition according to claim 1 wherein divalent metal cation is selected from the group consisting of Mg2+, Ca2+, Sr2+, Mn2+ and Zn2+.
5. A gassing composition according to any one of claims 1 to 4 wherein the anion, or anions, of the metal salt are selected from the group consisting of halide, nitrate, sulphate, phosphate, chlorate, perchlorate and combinations thereof.
6. A gassing composition according to claim 5 wherein the anion, or anions, of the metal salt is nitrate.
7. A gassing composition according to any one of claims 1 to 6 wherein the gassing agent is a nitrite salt.
8. A gassing composition according to claim 7 wherein the gassing agent is a sodium nitrite.
9. A gassing composition according to any one of claims 1 to 8 wherein the solution is an aqueous solution.
10. A gassing composition according to any one of claims 1 to 9 wherein said gassing composition comprises gassing agent between 0.5 wt% and 45 wt% of the gassing composition and divalent metal salt between 1 wt% and 45 wt% of the gassing composition.
11. A gassing composition according to claim 10 wherein said gassing composition comprises between 0.5 wt% and 25 wt% gassing agent and between 10 wt% and 40 wt% divalent metal salt.
12. A gassing composition according to any one of claims 1 to 11 including an accelerator.
13. A gassing composition according to claim 12 wherein the accelerator is a thiocyanate salt.
14. A gassing composition according to claim 13 wherein the thiocyanate salt is sodium thiocyanate.
15. A gassing composition according to any one of claims 12 to 14 wherein the accelerator forms from 0.05 wt % to 10 wt % of the gassing composition.
16. A method for gassing an emulsion explosive composition which comprises dispersing a gassing composition as claimed in any one of claims 1 to 15 into an explosive composition.
17. A method according to claim 16 wherein the gassing composition is dispersed in the explosive composition at a level of between 0.5 and 10 wt % of the total composition.
18. A method according to claim 17 wherein the gassing composition is dispersed in the explosive composition at a level of between 0.5 and 5 wt % of the total composition.
19. A method according to any one of claims 16 to 18 wherein the gassing composition is dispersed into the explosive composition by the use of static mixers.
20. A method according to any one of claims 16 to 19 wherein the explosive composition is a water-in-oil emulsion explosive.
21. A method according to claim 20 wherein the pH of an aqueous phase of the water-in-oil emulsion is adjusted to 4.2 prior to dispersion of the gassing composition in the explosive composition.
22. A gassed explosive composition comprising an emulsion explosive composition gassed by a method according to any one of claims 16 to 21.
23. An emulsion explosive composition comprising an emulsifier and gas bubbles formed from a gassing composition as claimed in any one of claims 1 to 15.
24. An explosive composition according to claim 23 wherein the ion is a calcium ion.
25. An explosive composition according to claim 23 wherein the ion is a strontium ion.
26. An explosive composition according to claim 23 or 24 wherein the calcium ion is derived from calcium nitrate or a mixture including calcium nitrate.
27. An explosive composition according to claim 23 or 25 wherein the strontium ion is derived from strontium nitrate, or a mixture including strontium nitrate.
28. An explosive composition according to claim 23 or 27 wherein the ion comprises a strontium ion and the nitrite salt is added as an aqueous solution containing the ion.
29. An explosive composition according to any one of claims 23 to 28 wherein the emulsifier is the reaction product of a polyisobutylene succinic anhydride (PiBSA) and an alkanolanime.
30. An explosive composition according to any one of claims 23 to 28 wherein the emulsifier is the condensation product of a poly[alk(en)yl] succinic anhydride with ethanolamine.
31. An explosive composition according to any one of claims 23 to 30 wherein the gassing composition forms between 0.5 and 10 wt % of the explosive composition and the gassing composition comprises between 0.5 and 45 wt % nitrite salt and between 1 and 45 wt % divalent metal salt.
32. An explosive composition according to any one of claims 23 to 31 wherein the gassing composition comprises a thiocyanate salt.
33. A method for gassing an emulsion explosive composition comprising adding to a pre-formed emulsion phase a gassing composition as claimed in any one of claims 1 to 15, and mixing the gassing composition uniformly throughout the emulsion phase to produce sensitizing gas bubbles.
34. A method according to claim 33 wherein the ion is a calcium ion.
35. A method according to claim 33 wherein the ion is a strontium ion.
36. A method according to claim 33 wherein the calcium ion is derived from calcium nitrate or a mixture including calcium nitrate.
37. A method according to claim 33 wherein the strontium ion is derived from strontium nitrate or a mixture including strontium nitrate.
38. A method according to claim 33 or 37wherein the ion comprises a strontium ion and the nitrite salt is added as an aqueous solution containing the ion.
39. A method according to any one of claims 33 to 38 wherein the emulsion phase comprises an emulsifier that is the reaction product of a polyisobutylene succinic anhydride (PiBSA) and an alkanolanime.
40. A method according to any one of claims 33 to 38 wherein the emulsion phase comprises an emulsifier that is the condensation product of a poly[alk(en)yl]
succinic anhydride with ethanolamine.
succinic anhydride with ethanolamine.
41. A method according to any one of claims 33 to 40 wherein the gassing composition forms between 0.5 and 10 wt % of the explosive composition and the gassing composition comprises between 0.5 and 45 wt % nitrite salt and between 1 and 45 wt % divalent metal salt.
42. A method according to any one of claims 33 to 40 wherein the gassing composition includes a thiocyanate salt.
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| AUPO8721A AUPO872197A0 (en) | 1997-08-22 | 1997-08-22 | Explosives gasser composition and method |
| AUPO8721 | 1997-08-22 | ||
| PCT/AU1998/000670 WO1999010299A1 (en) | 1997-08-22 | 1998-08-21 | Explosives gasser composition and method |
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| Country | Link |
|---|---|
| CN (1) | CN1271336A (en) |
| AU (1) | AUPO872197A0 (en) |
| BR (1) | BR9811346A (en) |
| CA (1) | CA2301552C (en) |
| WO (1) | WO1999010299A1 (en) |
| ZA (1) | ZA987559B (en) |
Cited By (1)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| RU2748152C2 (en) * | 2019-07-18 | 2021-05-19 | Общество с ограниченной ответственностью "СпецРешения" | Emulsion explosive composition and method for production thereof |
Families Citing this family (4)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| US6022428A (en) * | 1998-02-10 | 2000-02-08 | Dyno Nobel Inc. | Gassed emulsion explosive |
| US6515063B2 (en) | 2001-02-01 | 2003-02-04 | The Goodyear Tire & Rubber Company | Tire having colored tread |
| CN108911934A (en) * | 2018-08-13 | 2018-11-30 | 福建省民爆化工股份有限公司 | Foaming agent for emulsion explosive and the emulsion for using the foaming agent |
| CN108997070A (en) * | 2018-08-13 | 2018-12-14 | 福建省民爆化工股份有限公司 | A kind of Quick Foaming of Emulsion Explosives agent and emulsion |
Family Cites Families (3)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| AU2607688A (en) * | 1987-09-30 | 1989-04-18 | Mining Services International Corporation | Methods and compositions related to emulsified gassing agents for sensitizing explosive compositions |
| AUPN737295A0 (en) * | 1995-12-29 | 1996-01-25 | Ici Australia Operations Proprietary Limited | Gasser composition & method of gassing |
| AUPN737395A0 (en) * | 1995-12-29 | 1996-01-25 | Ici Australia Operations Proprietary Limited | Process and apparatus for the manufacture of emulsion explosive compositions |
-
1997
- 1997-08-22 AU AUPO8721A patent/AUPO872197A0/en not_active Abandoned
-
1998
- 1998-08-20 ZA ZA987559A patent/ZA987559B/en unknown
- 1998-08-21 CA CA2301552A patent/CA2301552C/en not_active Expired - Lifetime
- 1998-08-21 BR BR9811346-1A patent/BR9811346A/en not_active Application Discontinuation
- 1998-08-21 CN CN98809555A patent/CN1271336A/en active Pending
- 1998-08-21 WO PCT/AU1998/000670 patent/WO1999010299A1/en active IP Right Grant
Cited By (1)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| RU2748152C2 (en) * | 2019-07-18 | 2021-05-19 | Общество с ограниченной ответственностью "СпецРешения" | Emulsion explosive composition and method for production thereof |
Also Published As
| Publication number | Publication date |
|---|---|
| WO1999010299A1 (en) | 1999-03-04 |
| AUPO872197A0 (en) | 1997-09-18 |
| CA2301552A1 (en) | 1999-03-04 |
| CN1271336A (en) | 2000-10-25 |
| ZA987559B (en) | 1999-02-23 |
| BR9811346A (en) | 2000-09-12 |
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Legal Events
| Date | Code | Title | Description |
|---|---|---|---|
| EEER | Examination request | ||
| MKEX | Expiry |
Effective date: 20180821 |