US3095335A - Blasting agent of multi-sized and multidensity ammonium nitrate with fuel oil - Google Patents
Blasting agent of multi-sized and multidensity ammonium nitrate with fuel oil Download PDFInfo
- Publication number
- US3095335A US3095335A US16194A US1619460A US3095335A US 3095335 A US3095335 A US 3095335A US 16194 A US16194 A US 16194A US 1619460 A US1619460 A US 1619460A US 3095335 A US3095335 A US 3095335A
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- US
- United States
- Prior art keywords
- prills
- mixture
- fuel oil
- nitrate
- blasting agent
- Prior art date
- Legal status (The legal status 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 status listed.)
- Expired - Lifetime
Links
- PAWQVTBBRAZDMG-UHFFFAOYSA-N 2-(3-bromo-2-fluorophenyl)acetic acid Chemical compound OC(=O)CC1=CC=CC(Br)=C1F PAWQVTBBRAZDMG-UHFFFAOYSA-N 0.000 title claims description 23
- 238000005422 blasting Methods 0.000 title claims description 21
- 239000003795 chemical substances by application Substances 0.000 title claims description 16
- 239000000295 fuel oil Substances 0.000 title claims description 12
- 239000000203 mixture Substances 0.000 claims description 31
- 238000005474 detonation Methods 0.000 claims description 11
- 239000003921 oil Substances 0.000 claims description 11
- 230000000717 retained effect Effects 0.000 claims description 6
- 238000009826 distribution Methods 0.000 claims description 3
- 229910002651 NO3 Inorganic materials 0.000 claims description 2
- NHNBFGGVMKEFGY-UHFFFAOYSA-N Nitrate Chemical compound [O-][N+]([O-])=O NHNBFGGVMKEFGY-UHFFFAOYSA-N 0.000 claims description 2
- 239000008240 homogeneous mixture Substances 0.000 claims description 2
- 239000000843 powder Substances 0.000 description 10
- 239000002360 explosive Substances 0.000 description 8
- XLYOFNOQVPJJNP-UHFFFAOYSA-N water Substances O XLYOFNOQVPJJNP-UHFFFAOYSA-N 0.000 description 7
- 239000002245 particle Substances 0.000 description 6
- 238000004519 manufacturing process Methods 0.000 description 5
- 239000011369 resultant mixture Substances 0.000 description 4
- 239000010743 number 2 fuel oil Substances 0.000 description 3
- 238000003860 storage Methods 0.000 description 3
- 238000012935 Averaging Methods 0.000 description 2
- 239000005909 Kieselgur Substances 0.000 description 2
- VYPSYNLAJGMNEJ-UHFFFAOYSA-N Silicium dioxide Chemical compound O=[Si]=O VYPSYNLAJGMNEJ-UHFFFAOYSA-N 0.000 description 2
- 238000010521 absorption reaction Methods 0.000 description 2
- 239000000463 material Substances 0.000 description 2
- 238000000034 method Methods 0.000 description 2
- 238000010298 pulverizing process Methods 0.000 description 2
- 230000002411 adverse Effects 0.000 description 1
- 238000005054 agglomeration Methods 0.000 description 1
- 230000002776 aggregation Effects 0.000 description 1
- 238000006243 chemical reaction Methods 0.000 description 1
- 238000005553 drilling Methods 0.000 description 1
- 230000000694 effects Effects 0.000 description 1
- 238000004880 explosion Methods 0.000 description 1
- 239000003337 fertilizer Substances 0.000 description 1
- 239000000446 fuel Substances 0.000 description 1
- 239000004615 ingredient Substances 0.000 description 1
- 239000002184 metal Substances 0.000 description 1
- 238000005272 metallurgy Methods 0.000 description 1
- 238000005065 mining Methods 0.000 description 1
- 238000012986 modification Methods 0.000 description 1
- 230000004048 modification Effects 0.000 description 1
- 239000012254 powdered material Substances 0.000 description 1
- 239000007787 solid Substances 0.000 description 1
- 238000001179 sorption measurement Methods 0.000 description 1
- 239000007921 spray Substances 0.000 description 1
Classifications
-
- 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
- C06B31/285—Compositions containing an inorganic nitrogen-oxygen salt the salt being ammonium nitrate with fuel oil, e.g. ANFO-compositions
-
- 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
-
- 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
- Y10S149/115—Organic fuel
Definitions
- This invention relates generally to a blasting-agent mixture and method of making the same, and is especially concerned with blasting-agent mixtures containing prilled fertilizer-grade ammonium nitrate.
- blasting agent which is distinguished from an explosive in the narrow sense of the latter term by being non-cap-sensitive (incapable of being detonated with a single No. 8 blasting cap) and not subject to the stringent rules applying to the manufacture, transportation, storage, and bandling of explosives.
- fertilizer grade of ammonium nitrate has come into wide use in recent years as a blasting agent, especially in the coal-stripping industry, its popularity being due primarily to relatively low cost.
- the primary mode of use has been that of fertilizer-grade coated prills mixed with fuel oil.
- the prills are relatively porou having relatively low density of between .70 and .90, averaging about .82, and are highly hygroscopic, so as to be commonly coated to prevent the absorption of water, as with between 2% and 6% diatomaceous earth.
- the densities referred to herein are bulk densities as encountered in practical usage.
- the rate of detonation seldom exceeds 11,000 feet per second; which is insuificient velocity for many blasting purposes without closer spacing of the blastholes, which adds substantially to the drilling costs.
- coated prills As substantially all fertilizer-grade ammonium-nitrate prills have in the past been coated, as mentioned hereinbefore, to prevent agglomeration or caking due to the absorption of moisture, these relatively low-density porous prills will be referred to hereinafter as coated prills. Commonly the coated prills are of a spherical configuration and size to pass through -a 10-mesh screen and be retained on a ZO-mesh screen.
- fertilizer-grade ammonium-nitrate prills of relatively high density, between .90 and 1.1 and averaging about 1.0. These high-density ammonium-nitrate prills have heretofore been considered unusable for explosive purposes, being of a relatively dense, crystalline structure and having a smooth, glasslike surface so as to be incapable of absorbing suflicient oil for proper explosion.
- the method and resultant mixture of the instant invention produces a blasting agent of substantial density, approximating 1.1 so as to sink in water for blasting wet holes, and which has a very high velocity of detonation greater than 14,000 feet per second due principally to its relatively high density.
- the instant invention utilizes both the coated and uncoated prills of fertilizer-ghade ammonium nitrate. Stated generally, a quantity of coated prills is first mixed with oil, and a quantity of the uncoated prills is pulverized and the resultant powder immediately mixed with the coated prills and oil. Mechanically, this resultant mixture is relatively dense, as the powdered ammonium nitrate fills the voids between the prilled ammonium nitrate and increases the bulk density of the mixture to 1.1 in contrast to a bulk density of only .82 which obtained in all fertilizer-grade prill-oil mixtures used heretofore. The mixture is preferably vibrated to assume its maximum bulk density.
- the powdered high-density ammonium nitrate is of various-size particles, all of the particles passing through a 14-mesh screen, and some of the particles being retained on each of a 20-, 28-, 35-, 48-, 100-, and ZOO-mesh screen.
- the powder consisting of various-size particles advantageously fills the voids between the prills more completely and with a higher resultant density than .a powder consisting of uniformly sized particles.
- the pulverizing may be accomplished in a conventional hammer mill.
- 300 lbs. of coated ammoniumnitrate prills may be placed in a horizontal mixing machine and there sprayed with 18 lbs. of No. 2 fuel oil. Introduced on top of the coated prills and oil already in the mixer is 400 lbs. of the powdered relatively dense ammonium nitrate. Subsequently an additional 300 lbs. of coated ammonium-nitrate prills are placed on top of the 400 lbs. of powder, to sandwich the latter between lower and upper layers of prills. Then an additional 42 lbs. of No. 2 fuel oil is sprayed over all of the material and the mixer is operated until the ingredients are all thoroughly mixed.
- the mixture is bagged in any desired quantities.
- the mixture may be passed to a bagging hopper and there fed in 50-1b. quantities, or other desired quantities, into appropriately sized waterproof bags, a 50-lb. bag being of the order of 7 inches in diameter and about 31 inches long.
- the vibrator may be a standard platform vibrator with a pipe mounted on the platform of a size slightly larger than the bag diameter and slightly shorter than the length of the bag. With .the filled bag inserted in the pipe, the latter transmits vibration throughout its entire length to the cartridge causing the mixture to assume its maximum density.
- the bag is then closed by any suitable means, such as a wire tie at the top of the bag.
- the resultant mixture is of a density greater than 1, approximately equal to 1.1, to insure its sinking into a water-filled blasth'ole with the contents of the waterproof bag remaining dry.
- the mixture of the instant invention has a detonation velocity of 14,000 feet per second, and its brisance value or power is even more markedly increased, the brisant power varying as the square of the detonation velocity.
- the instant mixture is between 60% and 75% more powerful than any prior mixtures utilizing only fertilizer-grade ammonium nitrate and oil.
- the mixture is noncap-sensitive and classified as a blasting agent under the Code of the US. Bureau of Mines, so as to enjoy the safety and economic advantages thereof.
- the advantages of the present invention are obtainable with good blasting efficiency in varying the ratio by weight of coated prills to relatively dense powder between 35:65 and 70:30.
- the ratio of coated prills to powder be between 60:40 and 50:50.
- an oil content by 4 weight approximately 6% of the total mixture, permissible variation being between 3% and 9% by weight.
- the present invention provides a method of manufacturing a blasting agent, and the resultant mixture, which for the first time using only fertilizer-grade ammonium nitrate produces a mixture of density greater than 1.0, is free-running and resists caking for long periods of storage, possesses a detonation velocity of at least 14,000 feet per second without being cap sensitive, and which otherwise fully accomplishes its intended objects and is well adapted to meet practical conditions of manufacture, distribution, and use.
- a non-cap-sensitive blasting agent consisting essentially of a homogeneous mixture of relatively porous-coated fertilizer-grade ammonium-nitrate prills of a size to substantially completely pass through an 8-mesh screen and be retained on a 20-mesh screen, relatively dense crystalline powdered fertilizer-grade ammo- :nium nitrate of particle-size distribution to substantially completely pass through a 20-mesh screen and be at least partially retained on screens of 28, 35, 48, and 200 mesh, the ratio by weight of prills to powder being between 28:72 and 70:30, and fuel oil, the amount of oil being between 4% and 7% by weight of the total mixture, to define a free-flowing mixture having a density of at least 1.1 and a rate of detonation not less than 14,000 feet per second.
- a blasting agent according to claim 1 said porous coated prills being of an approximate bulk density between .7 and .9, and said powder being ground from crystalline prills having a bulk density of between .9 and 1.1.
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- Chemical & Material Sciences (AREA)
- Engineering & Computer Science (AREA)
- Chemical Kinetics & Catalysis (AREA)
- General Chemical & Material Sciences (AREA)
- Oil, Petroleum & Natural Gas (AREA)
- Inorganic Chemistry (AREA)
- Organic Chemistry (AREA)
- Fertilizers (AREA)
Description
3,095,335 Patented June 25, 1963 ice 3,095,335 BLASTING AGENT 6F MULTI-SIZED AND MULTI- giELNslTY AMMONHUM NETRATE WITH FUEL Don B. MeCloud and Dean E. Albon, Du Quoin, 111., as-
signors to Airmite-Midwest Incorporated, a corporation of Illinois No Drawing. Filed Mar. 21, 1960, Ser. No. 16,194 3 Claims. (Cl. 14921) This invention relates generally to a blasting-agent mixture and method of making the same, and is especially concerned with blasting-agent mixtures containing prilled fertilizer-grade ammonium nitrate.
While the mixture of the instant invention is explosive in its broad sense, the preferred embodiment disclosed hereinafter is technically more accurately termed a blasting agent, which is distinguished from an explosive in the narrow sense of the latter term by being non-cap-sensitive (incapable of being detonated with a single No. 8 blasting cap) and not subject to the stringent rules applying to the manufacture, transportation, storage, and bandling of explosives.
As is well-known, fertilizer grade of ammonium nitrate has come into wide use in recent years as a blasting agent, especially in the coal-stripping industry, its popularity being due primarily to relatively low cost. The primary mode of use has been that of fertilizer-grade coated prills mixed with fuel oil. The prills are relatively porou having relatively low density of between .70 and .90, averaging about .82, and are highly hygroscopic, so as to be commonly coated to prevent the absorption of water, as with between 2% and 6% diatomaceous earth. The densities referred to herein are bulk densities as encountered in practical usage. Due to the relatively low density of the agricultural or fertilizer-grade ammonium-nitrate prills, the rate of detonation seldom exceeds 11,000 feet per second; which is insuificient velocity for many blasting purposes without closer spacing of the blastholes, which adds substantially to the drilling costs.
Another disadvantage inherent in the prior usage of fertilizer-grade ammonium-nitrate prills as a blasting agent was the difiiculty or impossibility of loading water-filled blastholes. That is, the relatively low density of the mixture of fertilizer-grade ammonium nitrate and oil prevented its sinking to the bottom of such holes, and required the use of weights and similar devices in cartridges filled with the blasting mixture to insure that the cartridge would sink in water. Of course, these expedients substantially reduced the blasting efficiency of such cartridges. By the teachings of the instant invention a fertilizer-grade ammonium-nitrate mixture is obtained having a density greater than unity to insure its sinking to the bottom of Water-filled 'blastholes, Without the need for weights or the like, to considerably enhance the resultant efficiency and blasting effect.
As substantially all fertilizer-grade ammonium-nitrate prills have in the past been coated, as mentioned hereinbefore, to prevent agglomeration or caking due to the absorption of moisture, these relatively low-density porous prills will be referred to hereinafter as coated prills. Commonly the coated prills are of a spherical configuration and size to pass through -a 10-mesh screen and be retained on a ZO-mesh screen.
By recent manufacturing advances there have been produced fertilizer-grade ammonium-nitrate prills of relatively high density, between .90 and 1.1 and averaging about 1.0. These high-density ammonium-nitrate prills have heretofore been considered unusable for explosive purposes, being of a relatively dense, crystalline structure and having a smooth, glasslike surface so as to be incapable of absorbing suflicient oil for proper explosion.
These relatively dense, and hence nonporous fertilizergrade prills will be referred to hereinafter as uncoated prills.
While increased density of ammonium nitrate up to about 1.5 is conducive to increased rate of detonation or detonation velocity, it is essential that sufficient fuel oil be intimately contained in the mixture to support the reaction. The relatively dense uncoated prills were considered unusable in explosives as being insufficiently porous to absorb the required fuel oil. An important part of the instant invention resides in the discovery that upon pulverizing the relatively dense uncoated prills, the resulant po-wder or particles adsorb sufficient fuel oil to give proper explosive action. However, mere pulverizetion of the uncoated prills and mixture with fuel oil is unsatisfactory, as by the hygroscopic nature of the pulverized material it very soon cakes and forms a solid mass.
While the caking could be reduced by mixture with a considerable percentage of conditioner, such as diatomaceous earth or other inert powdered material, this adversely affects the explosive qualities and considerably reduces the detonation velocity. Another important discovery contributing to the success of the instant invention is that when the pulverized uncoated prills are mixed with coated prills and oil such mixture will not cake or harden, but remain loose and free-running during long periods of storage.
The method and resultant mixture of the instant invention produces a blasting agent of substantial density, approximating 1.1 so as to sink in water for blasting wet holes, and which has a very high velocity of detonation greater than 14,000 feet per second due principally to its relatively high density.
The instant invention utilizes both the coated and uncoated prills of fertilizer-ghade ammonium nitrate. Stated generally, a quantity of coated prills is first mixed with oil, and a quantity of the uncoated prills is pulverized and the resultant powder immediately mixed with the coated prills and oil. Mechanically, this resultant mixture is relatively dense, as the powdered ammonium nitrate fills the voids between the prilled ammonium nitrate and increases the bulk density of the mixture to 1.1 in contrast to a bulk density of only .82 which obtained in all fertilizer-grade prill-oil mixtures used heretofore. The mixture is preferably vibrated to assume its maximum bulk density.
More specifically, the uncoated relatively dense prills are ground to an approximate screen analysis as follows:
Total Percentage Screen Size (Tyler Mesh) On Passing Thus, it is seen that the powdered high-density ammonium nitrate is of various-size particles, all of the particles passing through a 14-mesh screen, and some of the particles being retained on each of a 20-, 28-, 35-, 48-, 100-, and ZOO-mesh screen. The powder consisting of various-size particles advantageously fills the voids between the prills more completely and with a higher resultant density than .a powder consisting of uniformly sized particles. The pulverizing may be accomplished in a conventional hammer mill.
By way of example, 300 lbs. of coated ammoniumnitrate prills may be placed in a horizontal mixing machine and there sprayed with 18 lbs. of No. 2 fuel oil. Introduced on top of the coated prills and oil already in the mixer is 400 lbs. of the powdered relatively dense ammonium nitrate. Subsequently an additional 300 lbs. of coated ammonium-nitrate prills are placed on top of the 400 lbs. of powder, to sandwich the latter between lower and upper layers of prills. Then an additional 42 lbs. of No. 2 fuel oil is sprayed over all of the material and the mixer is operated until the ingredients are all thoroughly mixed.
, It is preferred to spray the fuel oil on the prills rather than on the powder to insure that the prills receive their proper proportion of the fuel oil. Otherwise, the high adsorption of the powder would deprive the prills of the portion of the fuel oil necessary thereto.
After thorough mixing, the mixture is bagged in any desired quantities. By way of example, the mixture may be passed to a bagging hopper and there fed in 50-1b. quantities, or other desired quantities, into appropriately sized waterproof bags, a 50-lb. bag being of the order of 7 inches in diameter and about 31 inches long. After the 'bags are filled with the mixture, they are vibrated to settle the mixture in the bags. The vibrator may be a standard platform vibrator with a pipe mounted on the platform of a size slightly larger than the bag diameter and slightly shorter than the length of the bag. With .the filled bag inserted in the pipe, the latter transmits vibration throughout its entire length to the cartridge causing the mixture to assume its maximum density. The bag is then closed by any suitable means, such as a wire tie at the top of the bag.
The resultant mixture is of a density greater than 1, approximately equal to 1.1, to insure its sinking into a water-filled blasth'ole with the contents of the waterproof bag remaining dry. This eliminates the disadvantages of priorsart expediencies, such as the use of highly compressed ammonium nitrate which is difficult to detonate, and also the use of metal or concrete in a cartridge or bag which occupies space otherwise available for explosive or blasting agent.
Rather, by the instant method and resulting mixture, the entire space occupied is available to the blasting agent, and the latter is quite simply detonated, a single primer serving to detonate several cartridges even in .water-filled blastholes.
Moreover, the mixture of the instant invention has a detonation velocity of 14,000 feet per second, and its brisance value or power is even more markedly increased, the brisant power varying as the square of the detonation velocity. Hence, the instant mixture is between 60% and 75% more powerful than any prior mixtures utilizing only fertilizer-grade ammonium nitrate and oil.
Notwithstanding the considerably increased detonation velocity of the instant mixture, the mixture is noncap-sensitive and classified as a blasting agent under the Code of the US. Bureau of Mines, so as to enjoy the safety and economic advantages thereof.
By way of ranges and variations in proportions, the advantages of the present invention are obtainable with good blasting efficiency in varying the ratio by weight of coated prills to relatively dense powder between 35:65 and 70:30. However, it is preferred that the ratio of coated prills to powder be between 60:40 and 50:50. In
all cases, it is preferable to employ an oil content by 4 weight approximately 6% of the total mixture, permissible variation being between 3% and 9% by weight.
From the foregoing it is seen that the present invention provides a method of manufacturing a blasting agent, and the resultant mixture, which for the first time using only fertilizer-grade ammonium nitrate produces a mixture of density greater than 1.0, is free-running and resists caking for long periods of storage, possesses a detonation velocity of at least 14,000 feet per second without being cap sensitive, and which otherwise fully accomplishes its intended objects and is well adapted to meet practical conditions of manufacture, distribution, and use.
Although the present invention has been described in some detail by way of illustration and example for purposes of clarity of understanding, it is understood that certain changes and modifications may be made within the spirit of the invention and scope of the appended claims.
What is claimed is:
1. In a non-cap-sensitive blasting agent, the combination consisting essentially of a homogeneous mixture of relatively porous-coated fertilizer-grade ammonium-nitrate prills of a size to substantially completely pass through an 8-mesh screen and be retained on a 20-mesh screen, relatively dense crystalline powdered fertilizer-grade ammo- :nium nitrate of particle-size distribution to substantially completely pass through a 20-mesh screen and be at least partially retained on screens of 28, 35, 48, and 200 mesh, the ratio by weight of prills to powder being between 28:72 and 70:30, and fuel oil, the amount of oil being between 4% and 7% by weight of the total mixture, to define a free-flowing mixture having a density of at least 1.1 and a rate of detonation not less than 14,000 feet per second.
2. A blasting agent according to claim 1, said fuel oil being No. 2 fuel oil and uniformly distributed throughout the mixture.
3. A blasting agent according to claim 1, said porous coated prills being of an approximate bulk density between .7 and .9, and said powder being ground from crystalline prills having a bulk density of between .9 and 1.1.
References Cited in the file of this patent UNITED STATES PATENTS OTHER REFERENCES Cooley: Symposium on Mining Research, Missouri School of Mines and Metallurgy Bulletin, Technical Series No. 95, Nov. 14 and 15, 1957, pp. -125. (Copy in Scientific Library.) v
Claims (1)
1. IN A NON-CAP-SENSITIVE BLASTING AGENT, THE COMBINATION CONSISTING ESSENTIALLY OF A HOMOGENEOUS MIXTURE OF RELATIVELY POROUS-COATED FERTILIZER-GRADE AMMONIUM-NITRATE PRILLS OF A SIZE TO SUBSTANTIALLY COMPLETELY PASS THROUGH AN 8-MESH SCREEN AND BE RETAINED ON A 20-MESH SCREEN, RELATIVELY DENSE CRYSTALLINE POWDERED FERTILIZER-GRADE AMMOMIUM NITRATE OF PARTICLES-SIZE DISTRIBUTION TO SUBSTANTIALLY COMPLETELY PASS THROUGH A 20-MESH SCREEN AND BE AT LEAST PARTIALLY RETAINED ON SCREENS OF 28, 35, 48, 100 AND 200 MESH, THE RATIO BY WEIGHT OF PRILLS TO POWDER BEING BETWEEN 28:72 AND 70:30, AND FUEL OIL, THE AMOUNT OF OIL BEING BETWEEN 4% AND 7% BY WEIGHT OF THE TOTAL MIXTURE, TO DEFINE A FREE-FLOWNG MIXTURE HAVING A DENSITY OF AT LEAST 1.1 AND A RATE DETONATION NOT LESS THAN 14,000 FEET PER SECOND.
Priority Applications (1)
Application Number | Priority Date | Filing Date | Title |
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US16194A US3095335A (en) | 1960-03-21 | 1960-03-21 | Blasting agent of multi-sized and multidensity ammonium nitrate with fuel oil |
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Application Number | Priority Date | Filing Date | Title |
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US16194A US3095335A (en) | 1960-03-21 | 1960-03-21 | Blasting agent of multi-sized and multidensity ammonium nitrate with fuel oil |
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US3095335A true US3095335A (en) | 1963-06-25 |
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US16194A Expired - Lifetime US3095335A (en) | 1960-03-21 | 1960-03-21 | Blasting agent of multi-sized and multidensity ammonium nitrate with fuel oil |
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Cited By (10)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
US3180768A (en) * | 1962-10-15 | 1965-04-27 | Jr Edwin M Scott | Ammonium nitrate explosive composition containing calcium nitrate and oil |
US3200743A (en) * | 1963-10-24 | 1965-08-17 | Trojan Powder Co | Waterproof package for explosives |
US3303072A (en) * | 1965-05-26 | 1967-02-07 | Trojan Powder Co | Low density, nitrate-based explosive compositions |
US3305414A (en) * | 1963-07-25 | 1967-02-21 | Cominco Ltd | Method of comminuting ammonium nitrate prills mixed with hydrocarbon |
US3378417A (en) * | 1966-08-22 | 1968-04-16 | Mcferrin William Don | Explosive composition containing inorganic nitrate salt of particular size distribution |
US3394038A (en) * | 1967-04-25 | 1968-07-23 | Commercial Solvents Corp | Method of producing ammonium nitrate explosive compositions having high package densities |
US3453155A (en) * | 1968-01-22 | 1969-07-01 | Oriard Powder Co Inc | Blasting agent composition containing a hydrocarbon fuel and coated ammonium nitrate |
US3667388A (en) * | 1969-07-01 | 1972-06-06 | Robert W Heinemann | Explosive initiating devices |
US20050066835A1 (en) * | 2001-03-14 | 2005-03-31 | Anders Hafstrand | Propellant powder charge for barrel weapon |
WO2008029339A2 (en) * | 2006-09-04 | 2008-03-13 | African Explosives Limited | Explosive |
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Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
GB152199A (en) * | 1919-10-02 | 1920-10-14 | Mueller Ernst Kg | Improved process for the manufacture of ammonium nitrate explosives |
US2069612A (en) * | 1934-12-29 | 1937-02-02 | Du Pont | Blasting explosive |
US2124202A (en) * | 1936-12-03 | 1938-07-19 | Du Pont | Explosive |
US2602732A (en) * | 1947-09-10 | 1952-07-08 | Atlas Powder Co | Ammonium nitrate explosive |
US2703528A (en) * | 1953-11-05 | 1955-03-08 | Maumee Collieries Company | Blasting process |
US2752848A (en) * | 1953-02-19 | 1956-07-03 | Du Pont | Blasting explosive |
US2879133A (en) * | 1952-12-31 | 1959-03-24 | Standard Oil Co | Anticaking-agent for ammonium nitrate |
US2975046A (en) * | 1959-02-02 | 1961-03-14 | Spencer Chem Co | Ammonium nitrate explosive composition |
US2997378A (en) * | 1959-05-14 | 1961-08-22 | Atlas Chem Ind | Compacted ammonium nitrate |
US3013872A (en) * | 1959-08-31 | 1961-12-19 | Atlantic Refining Co | Waterproof ammonium nitrate explosive |
-
1960
- 1960-03-21 US US16194A patent/US3095335A/en not_active Expired - Lifetime
Patent Citations (10)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
GB152199A (en) * | 1919-10-02 | 1920-10-14 | Mueller Ernst Kg | Improved process for the manufacture of ammonium nitrate explosives |
US2069612A (en) * | 1934-12-29 | 1937-02-02 | Du Pont | Blasting explosive |
US2124202A (en) * | 1936-12-03 | 1938-07-19 | Du Pont | Explosive |
US2602732A (en) * | 1947-09-10 | 1952-07-08 | Atlas Powder Co | Ammonium nitrate explosive |
US2879133A (en) * | 1952-12-31 | 1959-03-24 | Standard Oil Co | Anticaking-agent for ammonium nitrate |
US2752848A (en) * | 1953-02-19 | 1956-07-03 | Du Pont | Blasting explosive |
US2703528A (en) * | 1953-11-05 | 1955-03-08 | Maumee Collieries Company | Blasting process |
US2975046A (en) * | 1959-02-02 | 1961-03-14 | Spencer Chem Co | Ammonium nitrate explosive composition |
US2997378A (en) * | 1959-05-14 | 1961-08-22 | Atlas Chem Ind | Compacted ammonium nitrate |
US3013872A (en) * | 1959-08-31 | 1961-12-19 | Atlantic Refining Co | Waterproof ammonium nitrate explosive |
Cited By (12)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
US3180768A (en) * | 1962-10-15 | 1965-04-27 | Jr Edwin M Scott | Ammonium nitrate explosive composition containing calcium nitrate and oil |
US3305414A (en) * | 1963-07-25 | 1967-02-21 | Cominco Ltd | Method of comminuting ammonium nitrate prills mixed with hydrocarbon |
US3200743A (en) * | 1963-10-24 | 1965-08-17 | Trojan Powder Co | Waterproof package for explosives |
US3303072A (en) * | 1965-05-26 | 1967-02-07 | Trojan Powder Co | Low density, nitrate-based explosive compositions |
US3378417A (en) * | 1966-08-22 | 1968-04-16 | Mcferrin William Don | Explosive composition containing inorganic nitrate salt of particular size distribution |
US3394038A (en) * | 1967-04-25 | 1968-07-23 | Commercial Solvents Corp | Method of producing ammonium nitrate explosive compositions having high package densities |
US3453155A (en) * | 1968-01-22 | 1969-07-01 | Oriard Powder Co Inc | Blasting agent composition containing a hydrocarbon fuel and coated ammonium nitrate |
US3667388A (en) * | 1969-07-01 | 1972-06-06 | Robert W Heinemann | Explosive initiating devices |
US20050066835A1 (en) * | 2001-03-14 | 2005-03-31 | Anders Hafstrand | Propellant powder charge for barrel weapon |
WO2008029339A2 (en) * | 2006-09-04 | 2008-03-13 | African Explosives Limited | Explosive |
WO2008029339A3 (en) * | 2006-09-04 | 2008-12-11 | African Explosives Ltd | Explosive |
AP2766A (en) * | 2006-09-04 | 2013-09-30 | Ael Mining Services Ltd Aeci | Explosive |
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