Explosive composition, method of making an explosive composition, and method of using an explosive composition

Information

  • Patent Grant
  • 7938920
  • Patent Number
    7,938,920
  • Date Filed
    Monday, October 17, 2005
    18 years ago
  • Date Issued
    Tuesday, May 10, 2011
    13 years ago
Abstract
An explosive composition is provided that is comprised of a Heavy ANFO and grain hulls. In one embodiment, the grain hulls are comprised of rice hulls. The grain hulls serve both as an inert bulking additive that reduces the density of the composition and as a sensitizer that reduces the energy needed to reliably detonate the composition. Also provided is a method for manufacturing an explosive composition comprised of Heavy ANFO and grain hulls, such as rice hulls. Additionally, a method of using an explosive comprised of ANFO and grain hulls in a mining operation is disclosed.
Description
FIELD OF THE INVENTION

The present invention relates to an explosive composition that comprises Heavy ANFO, a method for making the explosive composition, and a method for using the explosive composition.


BACKGROUND OF THE INVENTION

For many years, one of the most popular explosives for use in mining operations has been ammonium nitrate fuel oil (“ANFO”), which is formed of porous ammonium nitrate prills and diesel oil that is situated within the voids of the porous ammonium nitrate prills. In mining operations, the use of ANFO typically involves drilling a blast hole in the earth that is being mined. After a blast hole has been drilled, one or more initiators and ANFO are loaded into the blast hole. The ANFO is then detonated with the result being that the earth that is being mined is fractured in a manner that facilitates the removal of the earth by machinery for further processing. Typically, an array of blast holes is established and the ANFO established in the blast holes is detonated simultaneously or in a sequence that is designed to produce desired blast characteristics.


A drawback associated with ANFO is that it is highly absorbent and the absorption of water reduces the explosive capability of the ANFO. Consequently, ANFO is typically not used in situations in which water in a blast hole is likely to adversely affect the ANFO. The water can be water that is present in the blast hole when the ANFO is loaded and/or water that migrates into the blast hole after the ANFO has been loaded and before the ANFO is detonated. Due to ANFO's highly absorbent nature, ANFO is suitable for use in applications in which water is unlikely to meaningfully reduce the effectiveness of the ANFO. Additionally, when Ammonium Nitrate is mixed with Fuel Oil to form ANFO, the resulting composition is dry to the touch and, as a consequence, commonly referred to as a “Dry Mix” explosive.


To address the “wet blast hole” situation, a water resistant ANFO, commonly referred to as Heavy ANFO, was developed. Heavy ANFO is comprised of an emulsion explosive in combination with ANFO and/or ammonium nitrate prills. An emulsion explosive contains oxidizers that are dissolved in water droplets that are surrounded by an immiscible fuel, such as oil. Due to Heavy ANFO's water resistance, it is suitable for use in applications in which the composition will be exposed or is likely to be exposed to water. Additionally, Heavy ANFO is wet to the touch due to the interstices of the ammonium nitrated being filled within the ammonium nitrate with the emulsion explosive. Hence, Heavy ANFO is sometimes referred to as “wet mix” explosive.


In addition to water resistance, a given volume of Heavy ANFO has greater explosive energy than an equal volume of ANFO. In a mining situation, the greater explosive energy of Heavy ANFO per unit volume typically means that fewer blast holes need to be drilled to blast a particular area relative to the number of blast holes that need to be drilled when ANFO is used. Further, for a given explosive energy, the cost to produce Heavy ANFO is less than the cost to produce ANFO in many situations. Due to the increased explosive energy and reduced cost, Heavy ANFO is also utilized in dry blast hole situations.


A problem associated with Heavy ANFO is that the density of the Heavy ANFO in a blast hole increases with increasing depth in the blast hole. Stated differently, there is a density gradient for the Heavy ANFO in a blast hole. As the density of Heavy ANFO increases, the sensitivity of the Heavy ANFO decreases. Sensitivity is a measure of the amount of energy needed to reliably detonate an explosive. So, a more sensitive explosive requires less energy to detonate than a less sensitive explosive. Consequently, in a blast hole, the Heavy ANFO towards the bottom of the blast hole may be much less sensitive than the Heavy ANFO towards the top of the blast hole. This sensitivity gradient can produce asymmetrical or uneven detonations that fail to have the desired blast characteristics.


To address the density problem in Heavy ANFO, a number of solutions have been proposed. For instance, inert bulking agents in the form of certain agricultural waste products have been added to the Heavy ANFO. However, the agricultural waste products presently known to be used to reduce the density also reduce the sensitivity of the explosive, in many cases, to the point at which the explosive is ineffective. Another approach replaces some or all of the fuel oil in the Heavy ANFO with polystyrene. However, this approach also reduces the sensitivity of the explosive and is generally cost prohibitive. Yet another approach uses micro-balloons and/or perlite, which are known sensitizing agents, to decrease the density of the Heavy ANFO. This approach is not presently considered cost effective. A further approach uses chemical gassing to reduce the density. The drawback of this approach is that the density cannot be effectively controlled over a wide density range.


SUMMARY OF THE INVENTION

The present invention is directed to an explosive composition comprised of Heavy ANFO and a plant-derived, inert bulking and sensitizing additive. The explosive composition is wet to the touch and, as a consequence, is not considered a “dry mix” explosive. In one embodiment, the inert bulking and sensitizing additive comprises hulls of a grain, where each of the hulls has a plurality of voids. In addition, the inert bulking and sensitizing additive is substantially devoid of any components of the grain other than the hulls. In one embodiment, the hulls are rice hulls.


In another embodiment, the inert bulking and sensitizing additive comprises hulls of a grain that are each characterized by a plurality of voids. Further the hulls are no longer naturally attached to any other components of the grain. In one embodiment, the hulls are rice hulls. In other embodiments, the composition is substantially devoid of components of the grain other than the hulls of the grain.


Yet a further embodiment of the invention is directed to a method for making a Heavy ANFO with a plant-derived, inert bulking and sensitizing additive. The method, in one embodiment, comprises the steps of: (a) providing a blender; (b) loading the blender with an emulsion explosive; (c) after the emulsion explosive has been added to the blender, loading the blender with an ammonium nitrate based explosive; (d) using the blender to blend the emulsion explosive and the ammonium nitrate based explosive to create a Heavy ANFO; and (e) using the blender to blend the Heavy ANFO with an inert bulking and sensitizing additive comprising hulls of a grain, the hulls each characterized by a plurality of voids. In one embodiment, the hulls of grain comprise rice hulls.


An additional embodiment of the invention is directed to a method for making an explosive composition comprised of Heavy ANFO and hulls of a grain. The method comprises providing an end-to-end level blender and then using the blender to blend Heavy ANFO and the hulls of a grain to produce an explosive composition with a highly homogenous consistency. In a further embodiment, the blender is also used to blend the constituents of Heavy ANFO.


One other embodiment of the invention is directed to a method for using an explosive composition comprised of Heavy ANFO and hulls of a grain. The method comprises providing an explosive composition comprising Heavy ANFO and hulls of a grain and loading the explosive composition into a blast hole. In other embodiments, the method comprises blending a Heavy ANFO and the hulls of grain to produce the explosive composition and doing the blending on the property on which the blast hole is located. Yet a further embodiment comprises performing a blending of a Heavy ANFO and the hulls of grain on a mobile platform.







DETAILED DESCRIPTION

The present invention is directed to an explosive composition comprised of Heavy ANFO and a plant-derived, inert bulking and sensitizing additive.


Heavy ANFO is comprised of an emulsion explosive in combination with ANFO and/or ammonium nitrate. The emulsion explosive is comprised of: (a) a disperse phase with an aqueous solution of one or more oxidizer salts; and (b) a continuous phase with an oil and an emulsifying additive. Suitable oxidizer salts include ammonium nitrate, sodium nitrate, and calcium nitrate. Other oxidizers known to those skilled art or set forth in the literature relating to explosives are also feasible, including but not limited to Urea, iron oxide, lead dioxide, ammonium perchlorate, barium nitrate, barium peroxide, lead tetroxide, potassium chlorate, potassium chlorate, potassium perchlorate, sodium perchlorate, etc. Generally, the oxidizer or oxidizers are concentrated in the aqueous solution and can be saturated in the aqueous solution. The oil is typically fuel oil or diesel oil or a combination thereof. However, other oils known to those skilled in the art or set forth in the literature relating to explosives are feasible, including but not limited to waste oil, bunker oil, and mineral oil. Potential substitutes for oil are coal dust and rubber. Any one of a number of emulsifying additives known to those skilled in the art and set forth in the literature relating to explosives are feasible. Many suitable emulsifiers are characterized as esters or other derivatives of monhydric or polyhydric alcohols that are combined with long chain components or other lyophilic materials.


A typical explosive emulsion used in Heavy ANFO is comprised of from about 40% to about 80% by weight ammonium nitrate; from about 0% to about 40% by weight calcium nitrate; from about 0% to about 15% sodium nitrate; from about 10% to about 25% by weight water; and from about 5% to about 12% by weight fuel oil.


ANFO is comprised of ammonium nitrate and fuel oil. Typically, the ammonium nitrate is in the form of porous ammonium nitrate prills. However, other forms of ammonium nitrate can be utilized to produce ANFO, including but not limited to agricultural grade ammonium nitrate prills, crystalline ammonium nitrate, and ground ammonium nitrate. However, these other forms of ammonium nitrate typically result in a lower quality ANFO relative to ANFO made with porous ammonium nitrate prills. If desired, some of the ammonium nitrate can be replace with one or more other oxidizers, such as those noted with respect to the emulsion explosive. Fuel oil as used herein refers to any liquid petroleum product that is burned in a furnace for the generation of heat or used in an engine for the generation of power. In addition, the term fuel oil comprises: (a) suitable substitutes for such liquid petroleum products, such as mineral oils, and (b) combinations of such liquid petroleum products and suitable substitutes.


The plant derived, inert bulking and sensitizing additive comprises hulls of a grain with a characteristic of the hulls being that they each have a plurality of voids, commonly referred to as micro-voids due to their small size. The micro-voids serve to create what are known as “hot spots” or void volumes that, all other factors remaining constant, increase the sensitivity of the explosive composition. The hulls also, all other factors remaining constant, decrease the density of the explosive composition. Consequently, the hulls serve both to decrease density and increase sensitivity. In one embodiment, the additive comprises the hulls but is substantially devoid of any portion of the grain other than the hulls. In another embodiment, the explosive composition comprises the hulls but is substantially devoid of any portion of the grain other than the hulls, i.e., no portion of the grain other than the hull serves another purpose within the explosive composition. In yet a further variation, the additive comprises the hulls from the grain and another component that serves to reduce the density and/or increase the sensitivity of the explosive that is approximately the same size as a hull.


One type of hull that has a plurality of micro-voids and is capable of acting as an inert bulking agent to reduce the density of the explosive composition is a rice hull. The micro-void characteristic of rice hulls is discussed in Chapter 19 of Rice: Chemistry and Technology, written by Bienvenido O. Juliano, which is incorporated herein by reference. Rice hulls also have a waxy coating that complements the water resistant characteristic of the Heavy ANFO.


However, any other type of hull that exhibits micro-voids and is capable of acting as an inert bulking agent is also feasible.


The ranges of the raw materials for an explosive composition comprised of Heavy ANFO and a plant-derived, inert bulking and sensitizing additive is set forth in Table I.












TABLE I









Min. %
Max %











Raw Materials
by weight
















Ammonium nitrate
50
99



Calcium nitrate
1
 20*



Sodium nitrate
1
 20*



Fuel phase
1
10



Water
1.5
12



Inert bulking agent
1
 25**







*the combination of calcium nitrate and sodium nitrate has a maximum % of 20%



**% relative to final blend of Heavy ANFO and the hulls






It should be noted that the composition set forth in Table II assumes that an emulsion explosive is being utilized that comprises at least calcium nitrate and sodium nitrate. As previously noted emulsion explosives with other compositions are feasible.


The ranges of the raw materials for an embodiment of an explosive composition comprised of Heavy ANFO and a plant-derived, inert bulking and sensitizing additive that has characteristics that approach those of ANFO are set forth in Table II.












TABLE II








Range ± 1%



Raw Materials
by weight









Ammonium nitrate
75 



Calcium nitrate
12*



Sodium nitrate
12*



Fuel phase
  6.6



Water
  6.6



Inert Bulking Agent
 15**







*the combination of calcium nitrate and sodium nitrate has a maximum % of 12%



**% relative to final blend of Heavy ANFO and the hulls






The ranges of the raw materials for an embodiment of an explosive composition comprised of Heavy ANFO and a plant-derived, inert bulking and sensitizing additive that has characteristics that more closely approach those of ANFO is set forth in Table III.


More Preferred Constituents












TABLE III








Range ± 1%



Raw Materials
by weight



















Ammonium nitrate
75.23



Calcium nitrate
11.61*



Sodium nitrate
11.61*



Fuel phase
6.49



Water
6.58



Inert Bulking Agent
13.5**







*the combination of calcium nitrate and sodium nitrate has a maximum % of 11.61%



**% relative to final blend of Heavy ANFO and the hulls






Having described the explosive composition, a method for manufacturing the composition is now described. Generally, the explosive composition of a Heavy ANFO and a plant derived, inert bulking and sensitizing additive is formed in a blender. It is desirable to produce the explosive composition such that little mechanical stress is imparted to the constituents of the composition during the manufacturing process, but a high degree of homogeneity is achieved because this reduces the variability in the performance characteristics of the explosive composition. A mixer that has been found to be capable of producing the explosive composition with a high degree of homogeneity and to do so while causing little mechanical stress on the constituents of the composition is an end-to-end level blender. An example of such a blender is set forth in U.S. Pat. No. 4,506,990, which is incorporated herein by reference. Blenders that operate on similar principles to the blender set forth in the '990 patent are also feasible, as well as any blenders that are capable of achieving a high degree of homogeneity in the composition while subjecting the constituents of the composition to little stress during the manufacturing process. It should be appreciated that the explosive composition can be made and function as an explosive without having a high degree of homogeneity or having been subjected to little mechanical stress during the manufacturing process. However, if there is not a high degree of homogeneity and/or the composition is subject to significant mechanical stress during the manufacturing process the performance characteristics of the resulting composition are subject to a greater degree of variability.


The blender is implemented on a mobile platform to allow the explosive composition to be blended on the blast site and then transported between the various blast holes at the site. The blender is also equipped with directable chute, sleeve or auger that allows the explosive composition to be dispersed into the blast holes. It should be appreciated that the blender can be implemented on a stationary platform and then transferred to a mobile vehicle for transport to the blast holes. However, the transfer operation subjects the explosive to unnecessary mechanical stress that may adversely affect the performance of the composition.


Regardless of the type of blender that is utilized, the explosive composition is formed by blending Heavy ANFO and the plant derived, inert bulking and sensitizing additive comprised of hulls of grain with each of the hulls having a plurality of voids. More specifically, the inert bulking and sensitizing additive is added to Heavy ANFO that is present in the blender and blended with the Heavy ANFO. The blending is terminated when it appears that the hulls are substantially evenly distributed between the Heavy ANFO particles.


The Heavy ANFO in the blender can be produced at a different location and then loaded into the blender. However, in many cases, it is desirable to produce the Heavy ANFO in the same blender that is used to blend the Heavy ANFO with the bulking and sensitizing additive. In this case, the production of the explosive composition commences with the loading of an emulsion explosive into the blender. The emulsion explosive has a bulk density from about 1.26 gm/cc to about 1.50 gm/cc, an oxygen balance from about −7.5 to about 1.0. The emulsion explosive also has from about 10% to about 25% by weight water. The blender is typically not operative during the loading of the emulsion explosive.


After the emulsion explosive has been loaded into the blender, ANFO and/or ammonium nitrate is loaded into the blender. Typically, the blender is not operative during the loading of the ANFO and/or ammonium nitrate. At least in the case of an end-to-end level blender, the ANFO and/or ammonium nitrate is loaded such that it is on top of the previously loaded emulsion explosive. This reduces the mechanical stress placed on the ANFO and/or ammonium nitrate when the blender is activated because the rotors of the blender have been lubricated by the emulsion explosive.


After the ANFO and/or ammonium nitrate has been loaded into the blender, the blender is activated to blend the emulsion explosive with the ANFO and/or ammonium nitrate and thereby manufacture Heavy ANFO. In the case of an end-to-end level blender, the blending takes approximately two minutes. The Heavy ANFO has a bulk density from about 1.0 gm/cc to about 1.45 gm/cc. Heavy ANFO with a bulk density in this range, and especially with respect to the upper end of the range, is generally consider to be too dense to reliably detonate in certain applications.


After the Heavy ANFO has been produced, the inert bulking and sensitizing agent comprised of hulls that have voids is added to the Heavy ANFO in the blender and blended as described above. The blending of the additive with the Heavy reduces the bulk density of the explosive composition. Depending upon the amount of additive utilized, the resulting explosive composition has a bulk density from about 0.35 gm/cc to about 1.33 gm/cc. When an end-to-end level blender is used, blending of the Heavy ANFO followed by the blending of the Heavy ANFO with the inert bulking and sensitizing additive typically requires 4 to 12 minutes to complete.


The explosive composition is used in mining operations by loading the composition one or more blast holes together with an appropriate detonating device. Typically, the detonating device is loaded into a blast hole prior to the loading of the explosive composition into the blast hole. A blast engineer determines the amount of explosive that is to be loaded into each hole and a weighing system on the vehicle that transports the composition to the blast hole or holes is used to load the appropriate amount of the explosive composition in each hole. As previously, the explosive composition can be manufactured on the blast site. Further, the explosive composition can be manufactured on site and on a mobile vehicle that can then be used to transport the composition to the blast hole or holes.

Claims
  • 1. A method for making an explosive composition comprising: providing an end-to-end level blender;wherein said end-to-end level blender comprises: a mixer tank for holding at least two different materials that are to be blended together;a rotary structure for use in contacting at least two different materials within the mixer tank to facilitate the blending of the at least two different materials, the rotary structure having a first axis of rotation that is substantially parallel to a substantially planar upper surface of the materials that are to be blended when the mixing tank is substantially full of the materials and a first rotational portion for rotating about said first axis of rotation; anda drive for use in causing a first rotational portion to rotate about said first axis of rotation;using said end-to-end level blender to blend Heavy ANFO and an inert bulking and sensitizing additive comprising hulls of rice to achieve a high degree of homogeneity with little mechanical stress imparted to the Heavy ANFO and the inert bulking and sensitizing agent.
  • 2. A method, as claimed in claim 1, further comprising: using said end-to-end level blender to blend an emulsion explosive and an ammonium nitrate based explosive to create said Heavy ANFO.
  • 3. A method, as claimed in claim 1, wherein: during said step of using, said first rotational portion rotates about said first axis at less than 1000 revolutions per minute.
  • 4. A method, as claimed in claim 1, wherein: during said step of using, said first rotational portion rotates about said first axis at less than 500 revolutions per minute.
  • 5. A method, as claimed in claim 1, wherein: during said step of using, said first rotational portion rotates about said first axis at less than 100 revolutions per minute.
  • 6. A method, as claimed in claim 1, wherein: said rotary structure further comprises a second axis of rotation that is substantially parallel to first axis of rotation and a second rotational portion for rotating about said second axis of rotation.
  • 7. A method, as claimed in claim 6, wherein: during said step of using, said first rotational portion rotates about said first axis of rotation at a first rotational speed and said second rotational portion rotates about said second axis of rotation at a second rotational speed that is different than said first rotational speed.
  • 8. A method, as claimed in claim 7, wherein: during said step of using, said first rotational speed and said second rotational speed are each less than 500 revolutions per minute.
  • 9. A method, as claimed in claim 7, wherein: during said step of using, said first rotational speed and said second rotational speed are each less than 100 revolutions per minute.
  • 10. A method, as claimed in claim 6, wherein: during said step of using, said first rotational portion has a clockwise rotation about said first axis of rotation and said second rotational portion has a counter-clockwise rotation about said second axis of rotation.
  • 11. A method, as claimed in claim 6, wherein: said rotary structure further comprises a third axis of rotation that is substantially parallel to second axis of rotation and a third rotational portion for rotating about said third axis of rotation.
CROSS-REFERENCE TO RELATED APPLICATIONS

This application is a divisional of U.S. patent application Ser. No. 10/248,550, filed Jan. 28, 2003, which is incorporated by reference into this application in its entirety.

US Referenced Citations (37)
Number Name Date Kind
2344840 Watt et. al. Mar 1944 A
3356547 Berthmann et al. Dec 1967 A
3522117 Atadan et al. Jul 1970 A
3674578 Cattermole et al. Jul 1972 A
3770522 Tomic Nov 1973 A
4008108 Chrisp Feb 1977 A
4111727 Clay Sep 1978 A
4128442 Barlow Dec 1978 A
4138281 Olney et al. Feb 1979 A
4181546 Clay Jan 1980 A
4287010 Owen, II Sep 1981 A
4322258 Sudweeks et al. Mar 1982 A
4343663 Breza et al. Aug 1982 A
4364782 Funk et al. Dec 1982 A
4394199 Barnhard, IV et al. Jul 1983 A
4404050 Yorke et al. Sep 1983 A
4410378 Hattori et al. Oct 1983 A
4420349 Bampfield Dec 1983 A
4435232 Ciaramitaro et al. Mar 1984 A
4461660 Binet et al. Jul 1984 A
4470855 Bampfield Sep 1984 A
4472215 Binet et al. Sep 1984 A
4491489 Ellis et al. Jan 1985 A
4506990 Neier Mar 1985 A
4507161 Sujansky Mar 1985 A
4511412 Kakino Apr 1985 A
4511414 Matsui Apr 1985 A
4547232 Cartwright Oct 1985 A
4566919 Jessop Jan 1986 A
4594118 Curtin Jun 1986 A
4614146 Ross et al. Sep 1986 A
4875950 Waldock Oct 1989 A
4957569 Waldock Sep 1990 A
5409556 Lownds Apr 1995 A
6113715 Halander Sep 2000 A
6955731 Waldock Oct 2005 B2
20040231769 Bellairs et al. Nov 2004 A1
Foreign Referenced Citations (12)
Number Date Country
106877 Mar 1939 AU
110850 Mar 1941 AU
146182 Jan 1951 AU
166372 May 1953 AU
598130 Dec 1988 AU
621083 Aug 1989 AU
621994 Sep 1990 AU
661802 Aug 1995 AU
2004200628 Sep 2004 AU
2004212562 Apr 2005 AU
888102 Dec 1971 CA
1020358 Nov 1977 CA
Related Publications (1)
Number Date Country
20060289097 A1 Dec 2006 US
Divisions (1)
Number Date Country
Parent 10248550 Jan 2003 US
Child 11163380 US