NZ200238A - Water-in-oil emulsion blasting agent containing ca(no3)2 - Google Patents

Water-in-oil emulsion blasting agent containing ca(no3)2

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Publication number
NZ200238A
NZ200238A NZ20023882A NZ20023882A NZ200238A NZ 200238 A NZ200238 A NZ 200238A NZ 20023882 A NZ20023882 A NZ 20023882A NZ 20023882 A NZ20023882 A NZ 20023882A NZ 200238 A NZ200238 A NZ 200238A
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NZ
New Zealand
Prior art keywords
composition according
water
salt solution
weight
explosive composition
Prior art date
Application number
NZ20023882A
Inventor
A G Funk
H A Jessop
Original Assignee
Ireco Inc
Priority date (The priority date is an assumption and is not a legal conclusion. Google has not performed a legal analysis and makes no representation as to the accuracy of the date listed.)
Filing date
Publication date
Application filed by Ireco Inc filed Critical Ireco Inc
Priority to NZ20023882A priority Critical patent/NZ200238A/en
Publication of NZ200238A publication Critical patent/NZ200238A/en

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Description

New Zealand Paient Spedficaiion for Paient Number £00238 200238 Priority Date(s): Complete Specification Filed; Class: Publication Date: lU.junsasi P.O. Journal No: i?.ll NO SUBSTITUTION OF APPUCAST UNDER SECTION 24 \f\£c£7 iKiCcWoC-ftTE-C).
Number Dated EMULSION EXPLOSIVES CONTAINING /HIGH CONCENTRATIONS OF CALCIUM NITRATE I $We IKECO CHEMICALS', a corporation of the State of Utah, United States of America, of Seventh Floor, Kennecott Bldg., Salt Lake City, Utah, United States of America do hereby declare the invention for which' I£we pray that a Patent may be granted to IffiS/us. and the method by which it is to be performed, to be particularly described in and by the following statement: Patents 1-orm No. 5 PATENTS ACT. 1953 / / COMPLETE SPECIFICATION 1 '■itbhcmi ■ . ?;sc&med A need exists in the field for a small diameter, 75mm or less, water-in-oil emulsion blasting agent which is not cap-sensitive (to a No. 8 cap). It has been difficult to produce small diameter emulsion slurry explosives (those detonable in 75mm charge diameters or less) that are noncap-sensitive and yet remain reliably detonable in such small diameters. For example, the prior art discloses large diameter noncap-sensitive emulsion blasting agents which contain AN as the primary or sole oxidizing agent. If made sensitive enough to detonate reliably in small diameters, these prior art blasting agents generally would be cap-sensitive primarily due to the high amount of AN present. The present invention overcomes this problem by providing a water-in-oil emulsion slurry blasting agent that will reliably detonate in small diameters, but yet will remain noncap-sensitive. This property also enhances reliability of detonation in larger diameters as well. Thus the compositions of the present invention are useful in both small and large diameters. The high CN content of the compositions also makes them particularly advantageous for use in areas of the world where CN is more plentiful and thus more economical than AN. As used herein, the term blasting agent means a noncap-sensitive explosive.
The invention comprises a noncap-sensitive water-in-oil emulsion blasting agent having a water-immiscible liquid organic fuel as a continuous phase; an emulsified aqueous inorganic oxidizer salt solution as • *. a discontinuous phase, which salt solution contains a calcium nitrate to ammonium nitrate weight ratio of 1.5 or greater; an emulsifier; and optionally a density reducing agent. ;Most CN used in commercial blasting agents is fertilizer grade having about 15% by weight water of crystallization and about 6% AN. ;The amounts and percentages of CN referred to herein and in the appended claims are in reference to anhydrous CN. Thus if fertilizer grade CN is used, the amounts and percentages must be adjusted accordingly. ;\ . ' ;■The CN is present in an amount by weight equal 'to or greater than 1.5 times the amount of AN present. Thus, the weight ratio of CN to AN is 1.5 or greater. Preferably. the> ^ * ' 200238 to about 70% by weight based on the total composition. Correspondingly, the percentage of AN preferably is from 10% to about 33% by weight.
Minor amounts may be added of additional oxidizer salts selected from the group consisting of ammonium, alkali and alkaline earth metal nitrates, chlorates and perchlorates. The amount of total oxidizer salt employed is generally from about 45% to about 90% by weight of the total composition and preferably from about 60% to about 86%.
The use of high amounts of CN does not by itself insure that the blasting agent will remain noncap-senstitive. Sensitivity also depends upon other factors such as the amount of water present, the type of liquid organic fuel(s) used, the density of the blasting agent, the presence and type of sensitizer, and the amount and type of emulsifier. For example, as is well-known, the sensitivity of a blasting agent can be increased by adding a sensitizer, such as fine aluminum particles, by adjusting water content, or by lowering the density by the addition of density reducing agents such as fine, hollow glass spheres. Nevertheless, it is observed that as the CN:AN ratio is increased, and the other parameters and ingredients essentially are held constant, the blasting .agent will tend to remain noncap-sensitive even as the critical diameter correspondingly is decreased to relatively small diameters.
Water is employed in an amount from about 5% to about 20% by weight, based on the total composition.. It is preferably employed in amounts of from about 10% to about 16%. Water-miscible organic liquids can partially replace water as a solvent for the salts, and such liquids also function as a fuel for the composition. Moreover, certain organic liquids reduce the crystallization temperature of the oxidizer salts in solution.
Miscible liquid fuels can include alcohols such as methyl alcohol, glycols such as ethylene glycols, amides such as formamide, and analogous nitrogen-containing liquids. As is well known in the art, the amount'of total liquid used can vary according to the desired physical properties.
The immiscible liquid organic fuel forming the continuous phase of the composition is present in an amount of from about 3% to about 10%, 2 00238 and preferably in an amount of from about 4% to about 8%. The actual amount can be varied depending upon the particular immiscible fuel(s) used and upon the presence of other fuels, if any. When the immiscible fuel(s) is used as the sole fuel(s), it is preferably used in amount of from about 4% to about 8% by weight. The immiscible organic fuels can be aliphatic, alicyclic, and/or aromatic and can be saturated and/or unsaturated, so long as they are liquid at the formulation temperature. Preferred fuels include mineral oil, waxes, paraffin oils, benzene, toluene, xylenes, and mixtures of liquid hydrocarbons generally referred to as petroleum distillates such as gasoline, kerosene and diesel fuels. Particularly preferred liquid fuels are mineral oil, No. 2 fuel oil, paraffin waxes, and mixtures thereof. Aliphatic and aromatic nitrocompounds also can be used. Mixtures of any of the above and other fuels can be used.
Optionally, and in addition to the immiscible liquid organic fuel, solid or other^liquid fuels or both can be employed in selected amounts.
Examples of solid fuels which can be used are finely divided aluminum particles; finely divided carbonaceous materials such as gilsonite or coal; finely divided vegetable grain such as wheat; and sulfur. Misci-ble liquid fuels, also functioning as liquid extenders, are listed above. These additional solid and/or liquid fuels can be added generally in amounts ranging up to 15% by weight. If desired, undissolved oxidizer salt can be added to the composition along with any solid or liquid fuels.
The emulsifier of the present invention can be selected from those conventionally employed.
The emulsifier is employed in an amount of from about 0.2% to about 5% by weight. It preferably is employed in an amount of from about 1% to about 3%. Typical emulsifiers include sorbitan fatty acid esters, glycol esters, substituted oxazolines, alkyl amines or their salts, derivatives thereof and the like. Preferably the emulsifier contains an unsaturated hydrocarbon chain as its lipophilic portion, although the saturated form also can be used. 200238 It: has been found to be particularly advantageous to predissolve the emulsifier in the liquid organic fuel prior to adding the organic fuel to the aqueous solution. Preferably, the fuel and predissolved emulsifier are added to the aqueous solution at about the temperature of the solution. This method allows the emulsion to form quickly and with minimum agitation.
Sensitivity and stability of the compositions may be improved slightly by passing them through a high-shear system to break the dispersed phase into even smaller droplets prior to adding the density control agent.
In further illustration of the invention, the Table contains formulations and detonation results of preferred compositions (Examples A-D) of the present invention.
The examples clearly show the advantage of using a high CN content for making blasting agents having small critical diameters. The examples show that the higher the CN content, the lower the critical diameter that can be attained in a composition without making the composition overly sensitive to shock. Example A has the lowest density (which is inversely proportional to sensitivity), but because of the high content of CN, it remains noncap-sensitive and will detonate reliably even in diameters as small as 25 mm. Examples B and C have similar propoerties to Example A.
A comparison of Examples D and E further illustrates the effect of CN. At essentially equivalent densities of 1.14 and 1.15 g/cc, Examples D and E, respectively, illustrate the dramatic effect of using higher amounts of CN. Example D contains only slightly more CN but remains noncap-sensitive whereas Example E which contains less CN, is cap-sensitive. Example E is noncap-sensitive, however, at the higher density of 1.20. Examples F-H do not meet the required CN:AN ratio of greater than 1.5. Example F is cap-sensitive at a density of 1.24 and 2 00238 becomes noncap-sensitive only at a density of 1.28 and a larger critical diameter (32 mm). Example G is cap-sensitive even at a density of 1.36 and a higher critical diameter of 38 mm. Example H is cap-sensitive even though it has a critical diameter of 100 rim or more. In certain compositions, if the AN content is too high, cap-sensitivity cannot be avoided even at the natural density (using no density reducing agent) and though the critical diameter may be as high as 125 mm.
The compositions of the present invention can be used in the conventional manner. Although they normally are packaged, such as in cylindrical sausage form, in relatively small diameters, the compositions also can be loaded directly into boreholes as a bulk product. Thus the compositions can be used both as a small diameter and a large diameter product:. The compositions generally are extrudable and/or pumpable with conventional equipment. The above-described properties of the compositions render them versatile and economically advantageous for most applications.
While the present invention has been described with reference to certain illustrative examples and preferred embodiments, various modifications will be apparent to those skilled in the art and any such modifications are intended to be within the scope of the invention as set forth in the appended claims.
TABLE COMPOSITION INGREDIENTS (Parts by weight) CN a|n H^O (total) Enulslfier3 Liquid Organic15 D;ns1ty Reducing Agent0 Di»ns1ty (g/cc) Dotonation Results (5°C) Critical Diameter (mm) e Minimum Booster Sensitivity (ey (20°C)f 65 5 20 2 8 d 1.10 8g BA 57 15 19 2 8 d 1.12 8g BA 55 20 16 2 8 d 1.04/1.15 /32 8g/8g BA/BA 51 25 15 2 7 d 1.14 8g BA 47 30 14 2 7 d 1.15/1.20 /25 #12/8g HE/BA a b c d e f 40 39 13 2 6 d 1.24/1.28 /32 #12/8g HE/BA 32 49 11 2 6 d 1.36/1.46 38/50 8g/8g HE/BA 2-(8-heptadecenyl)-4, 4-bis(hydroxyn1ethyl)-2-oxazol1ne Mineral Oil • Hollow glass spheres from 3-M Company Amount that was necessary to reduce density to level Indicated "8g" represents an 8 gram pentolite booster; "#12" indicates the lowest blasting cap number that produced a detonation. "BA" stands for Blasting Aqent, indicating that little or no reaction occurred with a #8 cap at 20UC. "HE" stands for High Explosive, indicating that reaction or detonation occurred with a #8 cap at 20°C. 29 53 10 2 6 d 1.45 100 8g HE NJ NJ U 00 200238

Claims (10)

WHAT WE CLAIM IS:
1. A water-in-oil emulsion blasting agent comprising a water-immiscible liquid organic fuel as a continuous phase; an emulsified aqueous inorganic oxidizer salt solution as a discontinuous phase, which salt solution contains a calcium nitrate to ammonium nitrate weight ratio of 1.5 or greater; an emulsifier; and optionally a density reducing agent.
2. An explosive composition according to Claim 1 wherein the calcium nitrate is present in amount from 50% to 70% by. weight based on the total composition.
3. An explosive composition according to Claim 2 wherein the salt solution contains ammonium nitrate in an amount of from 10% to 33% by weight based on the total composition.
4. An explosive composition according to Claim 1 wherein the emulsifier is selected from the group consisting of sorbitan fatty acid esters, glycol esters, substituted oxazolines, alkyl amines or their salts, and derivatives thereof.
5. An explosive composition according to Claim 1 wherein the liquid organic fuel is selected from the group consisting of mineral oil, waxes, benzene, toluene, xylene, and petroleum distillates such as gasoline, kerosene, and diesel fuels.
6. An explosive composition according to Claim 5 wherein the liquid organic fuel is a mineral oil. 200238 -9-
7. An explosive composition according to Claim 1 wherein the density reducing agent is selected from the group consisting of small, hollow, dispersed glass or plastic spheres, perlite, a chemical foaming or gassing agent, and a combination of each.
8. An explosive composition according to Claim 7 wherein the density reducing agent is small, hollow, dispersed glass spheres.
9. A noncap-sensitive water-in-oil emulsion blasting agent comprising from 3% to 10% by weight based on the total composition of a water-immiscible liquid organic fuel as a continuous phase; an emulsified aqueous inorganic oxidizer salt solution as a discontinuous phase, which salt solution comprises calcium nitrate, ammonium nitrate and from 5% to 20% water by weight and in which the calcium nitrate to ammonium nitrate weight ratio is 1.5 or greater; from 0.2% to 5% of emulsifier by weight, and a density reducing agent in an amount sufficient to reduce the density of the composition to within the range from 1.0 to 1.4 g/cc.
10. An explosive composition according to Claim 9 wherein the oxidizer salt solution contains from 50% to 70% calcium nitrate by weight based on the total composition and from 10% to 33%"-ammonium nitrate by weight. KTUOBNEYS 6&R THE APPLICANT N,Z. PATENT OFFICE 13 MAR 1985 EECSjV'cS
NZ20023882A 1982-04-05 1982-04-05 Water-in-oil emulsion blasting agent containing ca(no3)2 NZ200238A (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
NZ20023882A NZ200238A (en) 1982-04-05 1982-04-05 Water-in-oil emulsion blasting agent containing ca(no3)2

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
NZ20023882A NZ200238A (en) 1982-04-05 1982-04-05 Water-in-oil emulsion blasting agent containing ca(no3)2

Publications (1)

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NZ200238A true NZ200238A (en) 1985-07-12

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