Classifications

• • B—PERFORMING OPERATIONS; TRANSPORTING
  • B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
  • B01J—CHEMICAL OR PHYSICAL PROCESSES, e.g. CATALYSIS OR COLLOID CHEMISTRY; THEIR RELEVANT APPARATUS
  • B01J2/00—Processes or devices for granulating materials, e.g. fertilisers in general; Rendering particulate materials free flowing in general, e.g. making them hydrophobic
  • B01J2/30—Processes or devices for granulating materials, e.g. fertilisers in general; Rendering particulate materials free flowing in general, e.g. making them hydrophobic using agents to prevent the granules sticking together; Rendering particulate materials free flowing in general, e.g. making them hydrophobic
• • C—CHEMISTRY; METALLURGY
  • C01—INORGANIC CHEMISTRY
  • C01C—AMMONIA; CYANOGEN; COMPOUNDS THEREOF
  • C01C1/00—Ammonia; Compounds thereof
  • C01C1/18—Nitrates of ammonium
• • C—CHEMISTRY; METALLURGY
  • C05—FERTILISERS; MANUFACTURE THEREOF
  • C05C—NITROGENOUS FERTILISERS
  • C05C1/00—Ammonium nitrate fertilisers
  • C05C1/02—Granulation; Pelletisation; Stabilisation; Colouring
• • C—CHEMISTRY; METALLURGY
  • C06—EXPLOSIVES; MATCHES
  • C06B—EXPLOSIVES OR THERMIC COMPOSITIONS; MANUFACTURE THEREOF; USE OF SINGLE SUBSTANCES AS EXPLOSIVES
  • C06B21/00—Apparatus or methods for working-up explosives, e.g. forming, cutting, drying
  • C06B21/0033—Shaping the mixture
  • C06B21/0066—Shaping the mixture by granulation, e.g. flaking
• • C—CHEMISTRY; METALLURGY
  • C06—EXPLOSIVES; MATCHES
  • C06B—EXPLOSIVES OR THERMIC COMPOSITIONS; MANUFACTURE THEREOF; USE OF SINGLE SUBSTANCES AS EXPLOSIVES
  • C06B31/00—Compositions containing an inorganic nitrogen-oxygen salt
  • C06B31/28—Compositions containing an inorganic nitrogen-oxygen salt the salt being ammonium nitrate
• • Y—GENERAL TAGGING OF NEW TECHNOLOGICAL DEVELOPMENTS; GENERAL TAGGING OF CROSS-SECTIONAL TECHNOLOGIES SPANNING OVER SEVERAL SECTIONS OF THE IPC; TECHNICAL SUBJECTS COVERED BY FORMER USPC CROSS-REFERENCE ART COLLECTIONS [XRACs] AND DIGESTS
  • Y10—TECHNICAL SUBJECTS COVERED BY FORMER USPC
  • Y10S—TECHNICAL SUBJECTS COVERED BY FORMER USPC CROSS-REFERENCE ART COLLECTIONS [XRACs] AND DIGESTS
  • Y10S149/00—Explosive and thermic compositions or charges
  • Y10S149/11—Particle size of a component
  • Y10S149/112—Inorganic nitrogen-oxygen salt

Definitions

• This invention relates to ammonium nitrate materials especially suitable for use in the filed of explosives and to methods for preparing such materials. More particularly, the invention relates to high density ammonium nitrate materials useful for the provision of explosives of improved efficiency.
• Ammonium nitrate based explosives are now widely employed and, for'example, are employed in strip mining operations where it is necessary to remove a sedimentary rock overlayer to expose the desired mineral values. Explosives of this type, when used for such operations, have the advantage that they are inexpensive and the advantage that they can be field mixed, but this does not mean that such explosives are ideal in all respects. To the contrary, ammonium nitrate based explosives, as commonly employed, have two pronounced disadvantages. The first of these disadvantages is that the detonation velocity of presently available ammonium nitrate explosives is considerably below the speed of sound in hard rock so that high efi'iciency is not obtained. The second such disadvantage is that the explosive compositions normally have such low densities that they will not sink when introduced into a water filled bore hole.
• Explosives based primarily upon ammonium nitrate in admixture with a suitable fuel are not at the present time widely employed in underground mining operations. There are a number of reasons for this but two primary importance are that this class of explosives usually has such a large critical diameter that they cannot be employed in small diameter bore holes and the detonation velocity of such explosives has not been high enough to give the desired results. As contrasted to the 8 to 10 inch diameter bore holes usually employed in strip mining, the bore holes used in underground mining are usually between 1 and 2 inches in diameter and this is below the minimum satisfactory size usable with conventional ammonium nitrate-fuel mixtures.
• Ammonium nitrate based explosives generally comprise ammonium nitrate granules, pellets or globules mixed with an amount of a suitable combustible fuel approximately sufficient to be oxidized by the decomposition of the ammonium nitrate, the most widely employed combustible fuels being liquid hydrocarbon mixtures, such as No. 2 fuel oil.
• Globules formed by solidification of suspended droplets are known in the art as prills and low density prilled ammonium nitrate is generally considered the best available form of ammonium nitrate for preparing explosives of the above type because the low density prills contain minute voids which permit the liquid hydrocarbon fuel to penetrate and become intimately associated with the ammonium nitrate.
• the minute voids also provide numerous compression centers which are believed to aid in the propagation of the explosion through adibatic compression of the gases con- 3,266,950 Patented August 16, 1966 tained in the voids to temperatures in excess of the ignition temperature of the ammonium nitrate-fuel mixture.
• a microprilled product which can have an appreciably higher bulk density than that of the high density fertilizer material mentioned above and, where desired, can have a density appreciably above that of water. It has been found that if microprills of proper sizes are selected, penetration of a fuel, such as hydrocarbon oil, to the interior portions of the prills is not necessary for an efiicient explosion and that the voids existing between the minute prills apparently serve as compression centers similarly to the internal voids of low density prills.
• a fuel such as hydrocarbon oil
• a microprilled product in accordance with this invention can be employed for producing an explosive which gives excellent results in bore holes of a diameter conventionally employed in underground mining operations.
• an explosive composition properly prepared from the microprilled product has a detonation velocity substantially above that of previously available hydrocarbonammonium nitrate mixtures and above the speed of sound in hard rock.
• ammonium nitrate particles in compositions according to this invention must comprise prills and cannot suitably consist of particles formed by grinding or the like. If high density fertilizer ammonium nitrate prills are ground, the resulting product is a relatively low density material which cannot readily be compressed to give bulk density comparable to that of the fertilizer grade material from which it was formed. Further, if the low density ground material is used to form an explosive mixture, the resulting mixture is characterized by a relatively low detonation velocity.
• ammonium nitrate cannot be microprilled by the techniques employed in the production of the abovementioned high density fertilizer prilled material for the reason that if one attempts to produce a product containing extremely small prills, the prills cohere so tenaciously as to make the product unsuitable for its intended use, and if one attempts to avoid this by the use of a parting agent, such large quantities of the agent are required to prevent prill cohesion that the utility of the resulting product in the explosives field is materially reduced if not destroyed.
• high density microprills of ammonium nitrate are produced by forming a molten mixture of ammonium nitrate and a hydratable inorganic material, the amount of the hydratable material being insufiicient to detract from the efiicient use of the finished product in compounding explosives.
• the amount of water in the mixture is then reduced, if such is necessary, below that capable of being taken up as water of hydration by the hydratable material and the thus dehydrated mixture is subjected to a prilling operation. It has been found that exceedingly small prills can readily be formed from such a mixture without any tendency for the prills to adhere to each other in an objectionable manner.
• a hydratable material is selected which imparts to the prills dimensional stability through variations in temperature normally encountered in storage so that disintegration of the prills in storage is substantially eliminated.
• the hydratable inorganic material which is mixed with ammonium nitrate in accordance with this invention an constitute any material which, at least in anhydrous form, is thermally stable at prilling temperatures and which readily forms a hydrate at lower temperatures.
• This does not mean that the hydrated or partially hydrated material cannot be thermally stable at prilling temperatures or that the anhydrous material could not suitably be capable of forming a hydrate at prilling or higher temperatures but only that the inorganic material must be capable of forming a hydrate with any free water in the ammonium nitrate mixture prior to the time that the prills would normally cohere in an objectionable manner.
• the hydratable material retain the prills substantially free of unbound water at temperatures within the range of C. to 45 C. which are usually encountered in storage.
• Simple hygroscopic inorganic salts as a class are suitable for use in accordance with this invention but the preferred hydratable materials are water soluble inorganic salts which form a hydrate in saturated air at a temperature of about 85 C. or higher.
• suitable materials are magnesium nitrate, 'alu minum nitrate, iron nitrate, calcium nitrate, zinc nitrate, magnesium sulfate, magnesium oxide and magnesium carbonate.
• oxides and carbonates that they 'are largely transformed to nitrates when added to molten ammonium nitrate.
• a hydratable material which imparts dimensional stability to the ammonium nitrate prills through a temperature range normally encountered by the prills in storage.
• Ammonium nitrate is capable of existing in several crystalline forms and normally undergoes a phase change at a temperature of about 32 C. This phase change is accompanied by a volume change which causes compacted forms of ammonium nitrate such as prills to crack or crumble internally and to eventually break down to a fine powder.
• the amount of the hydratable material employed must be at least sufiicient to chemically bind as water of hydration substantially all of the water in the ammonium nitrate mixture so that theoretically substantially no free water is present in the prilled material. Since it is almost impossible to retain the water in the ammonium nitrate mixture at a negligible level, one should normally employ, under even favorable conditions, at least about 0.02 percent by Weight, and preferably at least about 0.1 percent by weight, of the hydratable material.
• explosively inert material being defined to mean a material which neither decomposes to release oxygen nor is oxidizable to release energy under conditions of explosion.
• the amount of the hydratable material is retained below about 1% by weight of the mixture.
• the amount of water preesnt in the ammonium nitrate mixture at the time of prilling should not only be below the amount capable of being bound as water of hydration by the hydratable material in the mixture but should also be below the amount which would result in excessive explosive'ly inert material, as above defined, being present in the mixture.
• the water content, including Water of hydration at the time of prilling should be below about 5% by weight of the mixture and should preferably be below about 1% by weight of the mixture. If one desires prills which are dimensionally stable, the water content of the mixture at the time of prilling should be even lower and should in all such instances be below about 2% by weight and preferably below about 0.5% by weight of the mixture.
• the hydratable material can be introduced into the ammonium nitrate mixture by any desired procedure.
• solidified substantially anhydrous ammonium nitrate can be :mixed with the hydratable material while it is in a dehydrated condition and contains less than the normal amount of water of hydration, and the resulting mixture thereafter heated to a molten state and prilled.
• This procedure has the disadvantage that the hydratable materials suitable for use in this invention are frequently not available in a dehydrated form and the further disadvantage that the materials must be handled at all times under controlled humidity conditions.
• a procedure which is usually more satisfactory comprises preparing a relatively dilute solution of ammonium nitrate and adding the hydratable material in hydrated form to the ammonium nitrate solution.
• the resulting aqueous mixture can, in most instances, then be dehydrated by conventional procedures to a satisfactory water content.
• hydratable materials are advantageously employed which so tenaciously hold their water of hydration that special measures must be taken to reduce the water content of the ammonium nitrate mixture to a satisfactory level.
• the problem is further complicated by the fact that ammonium nitrate cannot be readily handled at temperatures normally necessary to result in the dehydration of many hydratable materials which otherwise have desirable characteristics for use in this invention.
• molten ammonium nitrate apparently facilitates the removal of water from such difficulty dehydratable hydrates and that dehydration can be effected under proper conditions at temperatures below the upper limit at which ammonium nitrate can be readily handled.
• temperatures in the range of to 210 C. and pressure below about 0.3 atmosphere
• an ammonium nitrate composition containing calcium nitrate, magnesium nitrate or a mixture of the two can readily be dehydrated to a water content of less than 0.5%.
• the terminal dehydration step can be carried out in any conventional manner but is advantageously carried out by evaporation fro-m thin films of the molten mixture using a tubular or wiped film evaporator.
• the prilling operation can be generally conventional and conventional apparatus can suitably be employed, but a few variations from normal equipment and procedure are advantageous.
• a spray nozzle is advantageously employed which produces microprills within a size range to be subsequently described.
• Spray nozzles of this type are commercially available and the selection of a suitable nozzle normally ptresents no difiiculties. If a spray head is selected which under the conditions employed provides prills having a proper range of particle sizes, no screening of the product will be required, although the particle size range of the product being produced should be checked at intervals.
• a further advantageous variation from the usual procedure comprises neutralizing the ammonium nitrate to remove any free acid present therein before prilling since the presence of free acid in the prills makes them more hygroscopic and sensitive to temperature changes.
• One consideration specific to the process of this invention is that the product must be cooled before appreciable caking has occurred to a temperature below that at which the hydratable material in the ammonium nitrate tends to form a hydrate so that the free water content of the prills is held at substantially zero level. This, however, need not necessitate a change in conventional prilling procedures because salts are readily available which tend to form hydrates at temperatures above those at which prills are conventionally removed from prilling towers.
• At least about 80% by weight of the prills must be of a size less than about 20 mesh.
• oversize prills are from 20 mesh the greater is the reduction in explosive efiiciency so that not only should the percentage by weight of oversize prills be held to a minimum but the degree to which the prills exceed 20 mesh in size should also be minimized.
• not more than about 5 to by weight of the prills should be below about 140 mesh in size because the presence of a large percentage of prills smaller than 140 mesh results in a reduction of bulk density, increased ca-king tendencies and reduced fiowa-bility. It is normally an advantage of ammonuim nitrate based explosives that they are relatively insensitive to detonation, but a product according to this invention containing greater than about 5 to 15% particles smaller than 140 mesh can, under favorable conditions, be readily detonated by a single primer cap. The presence of an excessive percentage of undersized particles also aggravates caking and reduces flowability.
• the prills should cover a substantial portion of the size range of from about to 140 mesh. This is because a prilled product in which the prills vary in size over an appreciable range is more dense than a product formed from prills of uniform size.
• the prill density and the range in prill size should be such that the product has a bulk density of at least about 60 or 62 and preferably of from about 68 to 75 pounds per cubic foot.
• the density of the individual prills is of no great importance except as it relates to bulk density, but because of this relationship the prills should have as near the theoretical maximum of 107 pounds per cubic foot as possible and should have a density of at least about 90 pounds per cubic foot. This is not difficult to achieve in accordance with the present invention, and, in fact, particle densities in excess of about 100 pounds per cubic foot can be routinely obtained.
• prill size For a prilled product with most desirable properties for use in holes of greater than about 3 inches in diameter, not only should the prill size extend over a substantial range but specific percentages of the prills preferably should be within various segments of the range of prill sizes.
• a product composed of particles predominantly less than about 140 mesh in size is generally advantageous in spite of the previously mentioned disadvantages of such a product. If great care is exercised to retain the product in a completely dry state, a product in accordance with this invention is satisfactory even when a major portion of the prills are so small that they cannot be classified by conventional screening techniques, or, in other words, less than about 325 mesh. Normally however, best results are obtained with a product in which at least 50 to of the prills are less than about 140 mesh with about 10 to 40% of the prills being smaller in size than 325 mesh. A wide range of particle sizes does not appear to be of primary importance with a product formed from such prills because other factors, such as a tendency to agglomerate, appear to have more effect upon bulk density than does particle size distribution.
• the prills be mixed with a suitable fuel.
• a suitable fuel such as carbon black, sawdust and oat hulls can be employed, but a liquid fuel such as a hydrocarbon oil permits a more intimate mixture and is much to be prefererd.
• the fuel may be mixed with the ammonium nitrate prills using any suitable equipment as illustrated by a rotary mixer.
• the amount of fuel mixed with ammonium nitrate prills to form an explosive is preferably an amount sufficient to exactly utilize the oxygen liberated by the decomposition of the nitrate. With the usual hydrocarbon oils this is about 6% by weight. If an amount of fuel either appreciably above or below the theoretically optimum amount is employed, the explosion efficiency of the composition is reduced and an eflicient explosion is not normally obtained if one employs less than about 3% or more than about 15% of a combustible fuel based on the weight of ammonium nitrate.
• An explosive composition prepared in accordance with this invention can be conventionally employed. Normally the mixture of fuel and ammonium nitrate is simply poured into a borehole, primed, fused and stemmed in the usual manner. If used in wet or water filled boreholes, the ammonium nitrate mixture is preferably packed in waterproof containers or the like to prevent moisture adsorption. Waterproof containers of a high density product prepared in accordance with this invention normally sink when placed in a water filled borehole and, as previously mentioned, this is a distinct advantage.
• EXAMPLE I of magnesium oxide are dissolved in 13.8 pounds of 55% nitric acid to form a solution of magnesium nitrate. This latter solution is filtered to remove any insoluble impurities and is then added to the aforementioned ammonium nitrate solution to give about 512 pounds of ammonium nitrate solution containing 1.75% magnesium nitrate and about 6% Water. This solution is passed rapidly through small diameter (e.g., 1 inch) tubes maintained at about 190 C., and is then allowed to flash into a chamber maintained at about 0.13 atmosphere pressure wherein water is vaporized from the composition to reduce the water content of the ammonium nitrate melt to about 0.3% H 0.
• small diameter e.g., 1 inch
• the thus concentrtaed ammonium nitrate is then prilled at a spray temperature of about 197 C., using a spray pressure and spray head such as to give prills of a size less than about 20 mesh but only about of which are smaller than 140 mesh.
• EXAMPLE II A concentrated molten ammonium nitrate mixture is prepared as in Example I and is atomized into a prilling tower to produce a product composed of prills of the following sizes:
• a prilled product prepared in accordance with this invention is especially useful in the field of explosives, it can also be employed to advantage in other instances.
• a dense, free-flowing, prilled ammonium nitrate product prepared in accordance 8.. with this invention can be employed to advantage as a source of oxygen in rocket propellant compositions.
• a prilled product in accordance with this invention can be advantageously employed in the fertilizer field for the reason that the free-flowing, small diameter prills can be readily and evenly distributed in the soil to be fertilized, or can be mixed with other fertilizer materials of similar particle size so that segregation is minimized.
• a free-flowing composition especially suitable for use in the field of explosives comprising from about 3% to 15% by Weight of a combustible liquid hydrocarbon fuel and ammonium nitrate, at least about by weight of which is present as prills of a size less than about 20 mesh, said prills containing between about 0.02% and about 1% by weight, calculated on an anhydrous basis, of a hydratable inorganic salt selected from the group consisting of magnesium nitrate, aluminum nitrate, iron nitrate, calcium nitrate, zinc nitrate, magnesium sulfate, magnesium oxide and magnesium carbonate and Water not in excess of about 1% by weight of water bound as Water of hydration by said hydratable salt, said prills having a mean prill density and a size distribution such that said composition has an uncompacted bulk density of at least about 60 pounds per cubic foot, the total amount of explosively inert materials in said composition being below about 6% by Weight.
• a free-flowing composition especially suitable for use in the field of explosives comprising from about 3% to 15 by weight of a combustible liquid hydrocarbon fuel and ammonium nitrate, at least about 90% of which is present as prills of a size less than about 20 mesh, said prills containing between about 0.02% and about 1% by weight calculated on an anhydrous basis of magnesium nitrate, and water not in excess of about 1% by weight of water bound as water of hydration by said hydratable salt, said prills having a mean prill density and a size distribution such that said composition has an uncompacted bulk density of at least about 60 pounds per cubic foot, the total amount of explosively inert materials in said composition being below about 6% by weight.
• a free-flowing composition especially suitable for use in the field of explosives comprising from about 3% to 15 by weight of a combustible liquid hydrocarbon fuel and ammonium nitrate, at least about 90% of which is present as prills of a size less than about 20 mesh, said prills containing between about 0.02% and about 1% by weight calculated on an anhydrous basis of calcium nitrate, and water not in excess of about 1% by weight of water bound as water of hydration by said hydratable salt, said prills having a mean prill density and a size distribution such that said composition has an uncompacted bulk density of at least about 60 pounds per cubic foot, the total amount of explosively inert meterials in said composition being below about 6% by weight.
• a free-flowing composition especially suitable for use in the field of explosives comprising from about 3% to 15 by weight of a combustible liquid hydrocarbon fuel and ammonium nitrate, at least about 90% by Weight of which is present as prills Within the size range of 20 to mesh, said prills containing between about 0.02% and about 1% by weight, calculated on an anhydrous basis, of a hydratable inorganic salt selected from the group consisting of magnesium nitrate, aluminum nitrate, iron nitrate, calcuim nitrate, zinc nitrate, magnesium sulfate, magnesium oxide and magnesium carbon-ate and water not in excess of about 1% by weight of Water bound as Water of hydration by said hydratable salt, said prills having a mean prill density and a size distribution such that said composition has an uncompacted bulk density of at least about 60 pounds per cubic foot, the total amount of explosively inert materials in said composition being below about 6% by Weight.
• a free-flowing composition especially suitable for use in the field of explosives comprising from about 3% to 15% by weight of a combustible liquid hydrocarbon fuel and ammonium nitrate, at least about 50% of which is present as prills of a size less than 140 mesh and from about 110% to 40% is present as prills of a size less than 325 mesh,'said prills containing between about 0.02% and about 1% by weight, calculated on an anhydrous basis, of a hydratable inorganic salt selected from the group consisting of magnesium nitrate, aluminum nitrate, iron nitrate, calcium nitrate, zinc nitrate, magnesium sulfate, magnesium oxide and magnesium carbonate and water not in excess of about 1% by Weight of water bound as water of hydration by said hydratable salt, said prills having a mean prill density and a size distribution such 2,988,437 5/1961 Stanley et al 149-46 3,061,488 10/1962 Scott

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• Chemical Kinetics & Catalysis (AREA)
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• 0
  • NL NL129384D patent/NL129384C/xx active
  • NL NL269156D patent/NL269156A/xx unknown
• 1961
  • 1961-09-04 GB GB31674/61A patent/GB988095A/en not_active Expired
  • 1961-09-11 DE DE1961M0050269 patent/DE1446886A1/de active Pending
• 1965
  • 1965-02-25 US US435330A patent/US3266960A/en not_active Expired - Lifetime

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