US3279965A - Ammonium nitrate explosive compositions - Google Patents
Ammonium nitrate explosive compositions Download PDFInfo
- Publication number
- US3279965A US3279965A US344821A US34482164A US3279965A US 3279965 A US3279965 A US 3279965A US 344821 A US344821 A US 344821A US 34482164 A US34482164 A US 34482164A US 3279965 A US3279965 A US 3279965A
- Authority
- US
- United States
- Prior art keywords
- ammonium nitrate
- density
- explosive
- liquid
- nitrate
- 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 69
- 239000000203 mixture Substances 0.000 title claims description 44
- 239000002360 explosive Substances 0.000 title claims description 43
- 239000007788 liquid Substances 0.000 claims description 27
- 238000001179 sorption measurement Methods 0.000 claims description 16
- 239000000463 material Substances 0.000 claims description 14
- 239000006260 foam Substances 0.000 claims description 13
- 229910002651 NO3 Inorganic materials 0.000 claims description 8
- NHNBFGGVMKEFGY-UHFFFAOYSA-N Nitrate Chemical compound [O-][N+]([O-])=O NHNBFGGVMKEFGY-UHFFFAOYSA-N 0.000 claims description 8
- 239000002245 particle Substances 0.000 description 15
- 239000004615 ingredient Substances 0.000 description 13
- 238000000034 method Methods 0.000 description 7
- 239000000123 paper Substances 0.000 description 7
- 239000000446 fuel Substances 0.000 description 6
- 239000007789 gas Substances 0.000 description 6
- 239000003921 oil Substances 0.000 description 6
- 239000013078 crystal Substances 0.000 description 5
- 238000005474 detonation Methods 0.000 description 5
- 238000002156 mixing Methods 0.000 description 5
- 239000000243 solution Substances 0.000 description 5
- 238000001704 evaporation Methods 0.000 description 4
- 238000004880 explosion Methods 0.000 description 4
- 238000004519 manufacturing process Methods 0.000 description 4
- QTBSBXVTEAMEQO-UHFFFAOYSA-N Acetic acid Chemical compound CC(O)=O QTBSBXVTEAMEQO-UHFFFAOYSA-N 0.000 description 3
- 239000004215 Carbon black (E152) Substances 0.000 description 3
- LFQSCWFLJHTTHZ-UHFFFAOYSA-N Ethanol Chemical compound CCO LFQSCWFLJHTTHZ-UHFFFAOYSA-N 0.000 description 3
- OKKJLVBELUTLKV-UHFFFAOYSA-N Methanol Chemical compound OC OKKJLVBELUTLKV-UHFFFAOYSA-N 0.000 description 3
- 238000013019 agitation Methods 0.000 description 3
- QVGXLLKOCUKJST-UHFFFAOYSA-N atomic oxygen Chemical compound [O] QVGXLLKOCUKJST-UHFFFAOYSA-N 0.000 description 3
- 239000006229 carbon black Substances 0.000 description 3
- 229930195733 hydrocarbon Natural products 0.000 description 3
- 150000002430 hydrocarbons Chemical class 0.000 description 3
- 229910052760 oxygen Inorganic materials 0.000 description 3
- 239000001301 oxygen Substances 0.000 description 3
- 238000012856 packing Methods 0.000 description 3
- 239000000126 substance Substances 0.000 description 3
- XLYOFNOQVPJJNP-UHFFFAOYSA-N water Substances O XLYOFNOQVPJJNP-UHFFFAOYSA-N 0.000 description 3
- QGZKDVFQNNGYKY-UHFFFAOYSA-O Ammonium Chemical compound [NH4+] QGZKDVFQNNGYKY-UHFFFAOYSA-O 0.000 description 2
- OKTJSMMVPCPJKN-UHFFFAOYSA-N Carbon Chemical compound [C] OKTJSMMVPCPJKN-UHFFFAOYSA-N 0.000 description 2
- 239000003463 adsorbent Substances 0.000 description 2
- 239000007864 aqueous solution Substances 0.000 description 2
- 229910052799 carbon Inorganic materials 0.000 description 2
- 239000003575 carbonaceous material Substances 0.000 description 2
- 229920002678 cellulose Polymers 0.000 description 2
- 239000001913 cellulose Substances 0.000 description 2
- 239000002283 diesel fuel Substances 0.000 description 2
- 238000011049 filling Methods 0.000 description 2
- 238000010304 firing Methods 0.000 description 2
- 239000008187 granular material Substances 0.000 description 2
- MHWLNQBTOIYJJP-UHFFFAOYSA-N mercury difulminate Chemical compound [O-][N+]#C[Hg]C#[N+][O-] MHWLNQBTOIYJJP-UHFFFAOYSA-N 0.000 description 2
- 238000002360 preparation method Methods 0.000 description 2
- 239000004576 sand Substances 0.000 description 2
- 239000007787 solid Substances 0.000 description 2
- 238000011282 treatment Methods 0.000 description 2
- VZSRBBMJRBPUNF-UHFFFAOYSA-N 2-(2,3-dihydro-1H-inden-2-ylamino)-N-[3-oxo-3-(2,4,6,7-tetrahydrotriazolo[4,5-c]pyridin-5-yl)propyl]pyrimidine-5-carboxamide Chemical compound C1C(CC2=CC=CC=C12)NC1=NC=C(C=N1)C(=O)NCCC(N1CC2=C(CC1)NN=N2)=O VZSRBBMJRBPUNF-UHFFFAOYSA-N 0.000 description 1
- 238000005422 blasting Methods 0.000 description 1
- 239000011248 coating agent Substances 0.000 description 1
- 238000000576 coating method Methods 0.000 description 1
- 238000005553 drilling Methods 0.000 description 1
- 238000001035 drying Methods 0.000 description 1
- 230000000694 effects Effects 0.000 description 1
- 230000008020 evaporation Effects 0.000 description 1
- 239000000295 fuel oil Substances 0.000 description 1
- 239000003502 gasoline Substances 0.000 description 1
- 239000004519 grease Substances 0.000 description 1
- 238000000227 grinding Methods 0.000 description 1
- 239000008240 homogeneous mixture Substances 0.000 description 1
- 239000002655 kraft paper Substances 0.000 description 1
- 150000007524 organic acids Chemical class 0.000 description 1
- 235000005985 organic acids Nutrition 0.000 description 1
- 239000011148 porous material Substances 0.000 description 1
- 230000000644 propagated effect Effects 0.000 description 1
- 239000011435 rock Substances 0.000 description 1
- 238000012216 screening Methods 0.000 description 1
- 238000003860 storage Methods 0.000 description 1
- 238000010998 test method Methods 0.000 description 1
Classifications
-
- C—CHEMISTRY; METALLURGY
- C06—EXPLOSIVES; MATCHES
- C06B—EXPLOSIVES OR THERMIC COMPOSITIONS; MANUFACTURE THEREOF; USE OF SINGLE SUBSTANCES AS EXPLOSIVES
- C06B45/00—Compositions or products which are defined by structure or arrangement of component of product
-
- 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
-
- C—CHEMISTRY; METALLURGY
- C06—EXPLOSIVES; MATCHES
- C06B—EXPLOSIVES OR THERMIC COMPOSITIONS; MANUFACTURE THEREOF; USE OF SINGLE SUBSTANCES AS EXPLOSIVES
- C06B47/00—Compositions in which the components are separately stored until the moment of burning or explosion, e.g. "Sprengel"-type explosives; Suspensions of solid component in a normally non-explosive liquid phase, including a thickened aqueous phase
Definitions
- This invention relates to the preparation of explosives which are composed of mixtures of ammonium nitrate with a combustible substance.
- Explosive compositions comprising mixtures of ammonium nitrate with dry combustible substances such as carbon black are known. These explosives are powerful in character but suffer from a number of limitations, and drawbacks. One major limitation is the necessity of using such explosives under conditions of close confinement in order to ensure that they fire. Thus, when these explosives are used for rock blasting, the explosives are usually put into a flexible container such as a bag which then must be tightly packed into a blast-hole; the blasthole must be carefully drilled and free from cracks, fissures, and the like, so that the flexible container will conform as closely as possible to the configuration of the hole so as to fill it completely.
- a general object of the invention is to provide explosives of this general character which will not have the limitations heretofore encountered.
- an object of the present invention is the production of improved explosive compositions prepared from ammonium nitfate and combustible ingredients, which will fire efiiciently without the requirement of being placed in a confined condition and which will not require the observance of other critical specifications as to their conditions of use particularly as to the minimum diameter.
- Another object of the invention is the production of explosive compositions the ingredients of which may be stored and transported separately and mixed into a homogeneous composition immediately prior to use whereby a number of hazards are eliminated.
- a further object of this invention is to provide improved explosive compositions, the ingredients of which will not require extensive and complicated physical or mechanical treatment. Additional objects of this invention will become evident in the following description.
- a new form of ammonium nitrate which has an especially porous, foam-like structure with a high power of adsorption.
- this form of ammonium nitrate is mixed with a combustible material which is liquid and free-flowing, an explosive composition is formed that will fire efliciently under the action of a primer or detonator even in com- 3,279,965 Patented Oct. 18, 1966 pletely unconfined conditions such as in free air.
- detonation of this explosive composition is even easier when it is in a confined condition.
- close confinement of this explosive is not a necessary requisite for the firing of this composition, so that the use of this explosive composition is facilitated and its range of applicability is greater extended.
- the liquid ingredient in the explosive composition of this invention may be any of a variety of combustible liquids or mixtures thereof, including liquid hydrocarbon fractions such as gasoline, fuel oil, gas oil, and the like; alcohol, such as ethanol, methanol, and the like; and organic acids such as acetic acid and the like.
- the proportion of the liquid ingredient to the total Weight of the composition that has been found satisfactory is from about 3% to about 12%, and a preferred range is from about 4% to about 8% by weight of liquid to the weight of the total composition.
- the porous foam-like ammonium nitrate is prepared by evaporating a thin layer of a concentrated aqueous solution of ammonium nitrate in a crystallizer at reduced pressure.
- the ammonium nitrate foams up and solidifies rapidly under these conditions into an especially porous, expanded structure having the appearance of foam and a very low density.
- the crystalline form of the ammonium nitrate prepared in this manner usually corresponds to the normally observed crystalline form of ammonium nitrate.
- the ammonium nitrate is in the orthorhombic form common at this temperature.
- the lattice structure of the crystals is changed by this procedure and the relative positions of the crystals are modified so that there are a great number of cavities left between the crystals.
- the ammonium nitrate thus foamed and expanded has a high porosity and a considerable specific surface due to its unique structure, which also results in an ammonium nitrate which has a low density and a high adsorption.
- a solution of approximately 92-95% ammonium nitrate in about 5-8% of water at a temperature of about 140 C. is placed in a 'crystallizer.
- a crystallizer which has a diameter of 1.40 meters, a height of 1 meter, and which is adapted to manufacture kg. of foamed ammonium nitrate
- about 68-70 cubic decirneters of solution is introduced into the apparatus, which produces a layer of solution of about 4-5 cm. depth.
- the crystallizer is then evacuated to a pressure of about 60 mm. of Hg and the water is evaporated quickly, which causes the ammonium nitrate to foam up.
- the ammonium nitrate foam thus produced is obtained as a cake which practically fills the crystallizer.
- the cake is then crushed and, if desired, the crushed particles are screened.
- the porous nitrate may be prepared in accordance with any other method and it may be used in the form of porous granules.
- the particle size of the foamed ammonium nitrate is chosen for convenience, inasmuch as the size of the particles used is relatively unimportant and the outer shape of the expanded ammonium nitrate is of minor importance.
- the important feature is the unique expanded structure of the nitrate. Since the fuel penetrates the pores of the expanded, porous nitrate, there is no critical size for the particles. For ease in handling, slightly crushed particles of the foamed ammonium nitrate are generally used. However, the particles are crushed only to the extent necessary to obtain a convenient particle size, and the particles retain the stable, foamed structure.
- Ammonium nitrate prepared in this Way has an apparent bulk density, in gram per cc. varying from about 0.1 to about 0.85 and an adsorption coefficient of gas oil of at least 8%. Ammonium nitrate having an adsorption coeflicient of about has been obtained. Since the adsorption phenomenon is a surface phenomenon, the rate of adsorption obviously changes with the density and the more the nitrate is expanded, the higher is the adsorption coefiicient. By adsorption coefiicient is meant the amount of liquid that can be adsorbed by the solid ammonium nitrate expressed in percent by weight of the liquid relative to the weight of ammonium nitrate.
- liquid fuel can be admixed therewith without particular agitation.
- the explosive composition is prepared with agitation, mixing is effected more rapidly than when no agitation is used.
- No special mixing equipment is needed; any apparatus adapted to mix two substances, one of which is solid'and the other liquid can be used.
- No particular precautions are required for the mixing operation other than normal safety precautions, such as avoiding open fires and avoiding temperatures above 150 C. for the ammonium nitrate. Since the mixing operation is simple, the two ingredients may be stored separately and combined only a short time before actual'use. In this way the hazards of storing and shipping the explosive mixture are eliminated.
- liquid ingredients usable in accordance with the invention are widely available, inexpensive, and the amounts required are comparatively low.
- suitable liquids for the purpose of the invention are inherently such that they will generally be found in large amounts on the work site, such as motor fuels.
- the preparation of an explosive, according to the invention will involve simply providing the foamed ammonium nitrate ingredients and bringing it to the site for use, Where it may then be mixed with a suitable amount of liquid fuel just before the explosive is required. This is a great practical advantage.
- the liquid combustible ingredient is well dispersed throughout the ammonium nitrate and coats a large amount of ammonium nitrate surface and it penetrates into the capillary ducts, so that a mixture of the foamed ammonium nitrate and fuel can be detonated relatively easily even in cartridges having a small diameter.
- detonation becomes easier. For example, in detonating an explosive mixture of 95% ammonium nitrate and 5% liquid fuel in a paper cartridge with a commercial number 8 primer which corresponds to 2 gr.
- the explosive mixture can be detonated in a paper cartridge having a diameter of 50 mm., if ammonium nitrate having a density of about 0.75 is used the explosive mixture can be detonated in a paper cartridge having a diameter of 40 mm., if ammonium nitrate having a density of 0.70 is used an explosive mixture can be detonated in a paper cartridge having a diameter of 30 mm., if the ammonium nitrate has a density of about 0.60 the explosive mixture can be detonated in a paper cartridge having a diameter of mm., and the size of the paper cartridge can be reduced still further for lower densities, to about 20 to 22 mm.
- the density should be chosen in accordance with the intended use. If small blast holes are provided, low densities should be used and for bigger blast holes higher densities should be employed. In order that the drilling of blast holes and the filling thereof be economical, it is advantageous to use the highest density which, for the diameter in question will lead to a safe and complete explosion. For general use, a density in the range of about 0.6 to about 0.75 is often preferable.
- the adsorption coeflicient of the ammonium nitrate may be increased by admixing with the nitrate a suitable amount of pulverulent carbonaceous material, such as carbon black, pulverized carbon, forms of cellulose such as soft sawdust and the like. This measure will at the same time prevent an undesirable setting of the ammonium nitrate.
- the maximum amount of carbonaceous material that should be admixed with the ammonium nitrate is the quantity which together with the combustible liquid ingredient just about completely utilizes the excess oxygen furnished by the ammonium nitrate.
- Example 1 1 kilogram of slightly crushed crystallized foamed am- 'monium nitrate (density not packed 0.654, density when A mixture is prepared of 1 kilogram of ammonium nitrate (light granules) having an apparent density of 0.420 Without packing, and an adsorption coefiicient of 15%, and 50 grams of diesel oil. After 1 hours rest the mixture is filled into cartridges consisting of kraft paper having a diameter of 30 mm. and a weight of g. The first cartridge is primed with a commercial No. 8-2 grams primer and is placed on a lead plate arranged on a support of sand. The second cartridge is equally placed on a lead plate, arranged on a support of sand.
- the extremities of the two cartridges are aligned, leaving a distance of 2 cm. between them. Explosion of the first cartridge is complete and entails the complete explosion of the second cartridge.
- the detonation rate of the second cartridge is 1,690 m. per second.
- Example 3 A mixture is prepared of 1 kilogram of ammonium nitrate prills, well dried (apparent density without packing 0.76, density after packing 0.80, less than 0.1% water,
- Example 4 An explosive mixture consisting of 93% of foamed, crushed ammonium nitrate having a density of 0.36 and 7% gas oil was prepare-d by mixing with a wooden spatula. The mixture was screened through a No. 8 sieve and the screened particles analyzed to determine the average particle size of the ammonium nitrate with the following results:
- the sieved mixture was introduced into sets of three tubular paper cartridge cases of 30 mm. diameter, of 52 mm. diameter and of 25 mm. diameter, the appropriate charge for each size cartridge case being used.
- the 30 mm. cartridge cases had a length of 15 cm. and when filled weighed an average of 51.5 gm.
- test cartridges aligned in the manner of the first sets but provided with an additional 1 cm. spacing between adjacent cartridges, the results were the same, the cartridges leaving three regular furrows.
- An improved explosive composition consisting essentially of 97%-88% porous ammonium nitrate foam havin a bulk density of about 0.1 to about 0.85 and an adsorption coefficient for gas oil of at least 8% and about 3% to 12% of a liquid combustible material substantially adsorbed on said ammonium nitrate.
- ammonium nitrate foam is the evaporation product of a concentrated solution of ammonium nitrate evaporated at less than atmospheric pressure.
- An improved explosive composition which consists essentially of about 88%-97% porous ammonium gnitrate foam having a density of about 0.1 to about 0.85, an adsorption coefficient for gas oil of at least 8%, and a large specific surface, and about 3% to 12% of an organic combustible material substantially adsorbed on said ammonium nitrate, coating a large amount of the surface of said ammonium nitrate and filling the capillary ducts.
- a stable explosive composition which consists essentially of about 88% to 97% of porous, expanded ammonium nitrate having a density of about 0.6 to about 0.75, an adsorption coefficient for gas oil of at least .8%, and a foam-like crystal or granular structure which has a large number of cavities among the crystals and thereby a large specific surface and about 3% to 12% of an organicliquid, combustible material substantially adsorbed on said ammonium nitrate.
- a method of preparing an improved explosive composition which comprises, evaporating a thin layer of concentrated ammonium nitrate solution at less than atmospheric pressure to obtain a stable porous ammonium nitrate foam having a density of about 0.1 to about 0.85, crushing said ammonium nitrate foam, and admixing about 88-97 parts by weight of said crushed ammonium nitrate foam wit-h about 3 to 12 parts by weight of an organic, liquid, combustible material.
- liquid combustible material is a liquid hydrocarbon.
- a method of preparing an improved explosive composition which comprises producing porous, expanded ammonium nitrate having a density of about 0.1 to about 0.85 and an adsorption coefficient of at least 8% by evaporating a thin layer of a 92% to 95% aqueous solution of ammonium nitrate at a temperature of about C. and at a pressure of about 60 mm. of Hg, and admixing about 88 to 92 parts by weight of said expanded ammonium nitrate with about 3 to 12 parts by Weight of a liquid, organic, combustible ingredient.
Landscapes
- Chemical & Material Sciences (AREA)
- Organic Chemistry (AREA)
- Crystallography & Structural Chemistry (AREA)
- Engineering & Computer Science (AREA)
- Chemical Kinetics & Catalysis (AREA)
- General Chemical & Material Sciences (AREA)
- Oil, Petroleum & Natural Gas (AREA)
- Inorganic Chemistry (AREA)
- Filling Or Discharging Of Gas Storage Vessels (AREA)
- Air Bags (AREA)
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| FR718703 | 1956-07-17 |
Publications (1)
| Publication Number | Publication Date |
|---|---|
| US3279965A true US3279965A (en) | 1966-10-18 |
Family
ID=8703397
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| US344821A Expired - Lifetime US3279965A (en) | 1956-07-17 | 1964-02-14 | Ammonium nitrate explosive compositions |
Country Status (2)
| Country | Link |
|---|---|
| US (1) | US3279965A (fr) |
| CH (1) | CH362957A (fr) |
Cited By (13)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| US3378415A (en) * | 1964-10-12 | 1968-04-16 | Commercial Solvents Corp | Explosive slurry containing an agglom-erate of an inorganic nitrate oxidizer and a fuel and method of making |
| US3388014A (en) * | 1966-05-27 | 1968-06-11 | Chemical & Ind Corp | Ammonium nitrate explosive and process for producing same |
| US3450582A (en) * | 1967-12-18 | 1969-06-17 | Harold W Sheeran | Aqueous ammonium nitrate blasting composition containing solid carbonaceous fuel and method of preparing same |
| US3619305A (en) * | 1968-02-26 | 1971-11-09 | Explosifs Prod Chim | Explosive compositions containing expanded ammonium nitrate in crystalline form and method of preparing same |
| US3790415A (en) * | 1970-08-18 | 1974-02-05 | Du Pont | Chemical foaming and sensitizing of water-bearing explosives with hydrogen peroxide |
| US3830672A (en) * | 1966-08-30 | 1974-08-20 | Aerojet General Co | Solid porous, coated oxidizer, method of preparation and novel propellant compositions |
| US4093478A (en) * | 1972-12-07 | 1978-06-06 | Tyler Holding Company | Activated ammonium nitrate explosive composition |
| US5041177A (en) * | 1990-05-07 | 1991-08-20 | Eti Explosives | Ammonium nitrate/fuel oil blasting explosive having decreased oil segregation |
| US5480500A (en) * | 1994-10-24 | 1996-01-02 | Eti Explosives | Ammonim nitrate fuel oil blasting composition having improved water resistance |
| US5925846A (en) * | 1994-10-24 | 1999-07-20 | Eti Canada | Method for the production of an ammonium nitrate fuel oil blasting composition having improved water resistance |
| US6113714A (en) * | 1998-04-29 | 2000-09-05 | Eti Canada Inc. | Ammonium nitrate fuel oil blasting composition having improved water resistance |
| RU2334733C1 (ru) * | 2007-04-10 | 2008-09-27 | Общество с ограниченной ответственностью Научно-техническая фирма "Взрывтехнология" | Способ заряжания скважин взрывчатыми веществами на основе гранулированной аммиачной селитры |
| RU2465550C1 (ru) * | 2011-05-17 | 2012-10-27 | Общество с ограниченной ответственностью Научно-техническая фирма "Взрывтехнология" | Способ определения относительной работоспособности взрывчатого вещества |
Families Citing this family (1)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| DE1244031B (de) * | 1963-07-15 | 1967-07-06 | Karl Porr | Rieselfaehiges, im wesentlichen aus Ammoniumnitrat bestehendes Sprengstoffgemisch |
Citations (3)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| US2125161A (en) * | 1936-07-18 | 1938-07-26 | Du Pont | Ammonium nitrate explosive |
| US2174238A (en) * | 1936-07-18 | 1939-09-26 | Du Pont | Manufacture of ammonium nitrate |
| GB839078A (en) * | 1958-02-04 | 1960-06-29 | Canadian Ind | Ammonium nitrate explosives and their manufacture |
-
1957
- 1957-07-15 CH CH4847057A patent/CH362957A/fr unknown
-
1964
- 1964-02-14 US US344821A patent/US3279965A/en not_active Expired - Lifetime
Patent Citations (3)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| US2125161A (en) * | 1936-07-18 | 1938-07-26 | Du Pont | Ammonium nitrate explosive |
| US2174238A (en) * | 1936-07-18 | 1939-09-26 | Du Pont | Manufacture of ammonium nitrate |
| GB839078A (en) * | 1958-02-04 | 1960-06-29 | Canadian Ind | Ammonium nitrate explosives and their manufacture |
Cited By (13)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| US3378415A (en) * | 1964-10-12 | 1968-04-16 | Commercial Solvents Corp | Explosive slurry containing an agglom-erate of an inorganic nitrate oxidizer and a fuel and method of making |
| US3388014A (en) * | 1966-05-27 | 1968-06-11 | Chemical & Ind Corp | Ammonium nitrate explosive and process for producing same |
| US3830672A (en) * | 1966-08-30 | 1974-08-20 | Aerojet General Co | Solid porous, coated oxidizer, method of preparation and novel propellant compositions |
| US3450582A (en) * | 1967-12-18 | 1969-06-17 | Harold W Sheeran | Aqueous ammonium nitrate blasting composition containing solid carbonaceous fuel and method of preparing same |
| US3619305A (en) * | 1968-02-26 | 1971-11-09 | Explosifs Prod Chim | Explosive compositions containing expanded ammonium nitrate in crystalline form and method of preparing same |
| US3790415A (en) * | 1970-08-18 | 1974-02-05 | Du Pont | Chemical foaming and sensitizing of water-bearing explosives with hydrogen peroxide |
| US4093478A (en) * | 1972-12-07 | 1978-06-06 | Tyler Holding Company | Activated ammonium nitrate explosive composition |
| US5041177A (en) * | 1990-05-07 | 1991-08-20 | Eti Explosives | Ammonium nitrate/fuel oil blasting explosive having decreased oil segregation |
| US5480500A (en) * | 1994-10-24 | 1996-01-02 | Eti Explosives | Ammonim nitrate fuel oil blasting composition having improved water resistance |
| US5925846A (en) * | 1994-10-24 | 1999-07-20 | Eti Canada | Method for the production of an ammonium nitrate fuel oil blasting composition having improved water resistance |
| US6113714A (en) * | 1998-04-29 | 2000-09-05 | Eti Canada Inc. | Ammonium nitrate fuel oil blasting composition having improved water resistance |
| RU2334733C1 (ru) * | 2007-04-10 | 2008-09-27 | Общество с ограниченной ответственностью Научно-техническая фирма "Взрывтехнология" | Способ заряжания скважин взрывчатыми веществами на основе гранулированной аммиачной селитры |
| RU2465550C1 (ru) * | 2011-05-17 | 2012-10-27 | Общество с ограниченной ответственностью Научно-техническая фирма "Взрывтехнология" | Способ определения относительной работоспособности взрывчатого вещества |
Also Published As
| Publication number | Publication date |
|---|---|
| CH362957A (fr) | 1962-06-30 |
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