US3926698A - Explosive compositions containing metallic fuel particles and method of preparation thereof - Google Patents
Explosive compositions containing metallic fuel particles and method of preparation thereof Download PDFInfo
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- US3926698A US3926698A US444691A US44469174A US3926698A US 3926698 A US3926698 A US 3926698A US 444691 A US444691 A US 444691A US 44469174 A US44469174 A US 44469174A US 3926698 A US3926698 A US 3926698A
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- solution phase
- metallic particles
- sensitivity
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- 239000000203 mixture Substances 0.000 title claims abstract description 92
- 239000002360 explosive Substances 0.000 title claims abstract description 46
- 239000000446 fuel Substances 0.000 title claims abstract description 26
- 238000000034 method Methods 0.000 title claims description 22
- 239000002245 particle Substances 0.000 title abstract description 29
- 238000002360 preparation method Methods 0.000 title description 3
- 230000035945 sensitivity Effects 0.000 claims abstract description 33
- 238000005422 blasting Methods 0.000 claims abstract description 15
- 150000003839 salts Chemical class 0.000 claims abstract description 15
- 239000012530 fluid Substances 0.000 claims abstract description 14
- 239000007800 oxidant agent Substances 0.000 claims abstract description 13
- 238000005188 flotation Methods 0.000 claims description 34
- 229910052782 aluminium Inorganic materials 0.000 claims description 28
- XAGFODPZIPBFFR-UHFFFAOYSA-N aluminium Chemical compound [Al] XAGFODPZIPBFFR-UHFFFAOYSA-N 0.000 claims description 28
- 239000007788 liquid Substances 0.000 claims description 23
- 239000013528 metallic particle Substances 0.000 claims description 22
- ZQPPMHVWECSIRJ-KTKRTIGZSA-N oleic acid Chemical compound CCCCCCCC\C=C/CCCCCCCC(O)=O ZQPPMHVWECSIRJ-KTKRTIGZSA-N 0.000 claims description 21
- WRIDQFICGBMAFQ-UHFFFAOYSA-N (E)-8-Octadecenoic acid Natural products CCCCCCCCCC=CCCCCCCC(O)=O WRIDQFICGBMAFQ-UHFFFAOYSA-N 0.000 claims description 19
- LQJBNNIYVWPHFW-UHFFFAOYSA-N 20:1omega9c fatty acid Natural products CCCCCCCCCCC=CCCCCCCCC(O)=O LQJBNNIYVWPHFW-UHFFFAOYSA-N 0.000 claims description 19
- QSBYPNXLFMSGKH-UHFFFAOYSA-N 9-Heptadecensaeure Natural products CCCCCCCC=CCCCCCCCC(O)=O QSBYPNXLFMSGKH-UHFFFAOYSA-N 0.000 claims description 19
- ZQPPMHVWECSIRJ-UHFFFAOYSA-N Oleic acid Natural products CCCCCCCCC=CCCCCCCCC(O)=O ZQPPMHVWECSIRJ-UHFFFAOYSA-N 0.000 claims description 19
- QXJSBBXBKPUZAA-UHFFFAOYSA-N isooleic acid Natural products CCCCCCCC=CCCCCCCCCC(O)=O QXJSBBXBKPUZAA-UHFFFAOYSA-N 0.000 claims description 19
- 239000005642 Oleic acid Substances 0.000 claims description 18
- 235000014113 dietary fatty acids Nutrition 0.000 claims description 18
- 239000000194 fatty acid Substances 0.000 claims description 18
- 229930195729 fatty acid Natural products 0.000 claims description 18
- 150000004665 fatty acids Chemical class 0.000 claims description 14
- 229920002050 silicone resin Polymers 0.000 claims description 6
- 239000000344 soap Substances 0.000 claims description 6
- 229920001451 polypropylene glycol Polymers 0.000 claims description 5
- XNWFRZJHXBZDAG-UHFFFAOYSA-N 2-METHOXYETHANOL Chemical compound COCCO XNWFRZJHXBZDAG-UHFFFAOYSA-N 0.000 claims description 4
- 125000005313 fatty acid group Chemical group 0.000 claims description 4
- 230000006872 improvement Effects 0.000 claims description 2
- 230000001590 oxidative effect Effects 0.000 claims description 2
- 239000002002 slurry Substances 0.000 abstract description 17
- 238000005474 detonation Methods 0.000 abstract description 11
- 239000006185 dispersion Substances 0.000 abstract description 5
- 238000004519 manufacturing process Methods 0.000 abstract description 2
- 239000000243 solution Substances 0.000 description 42
- 239000007789 gas Substances 0.000 description 28
- 238000000576 coating method Methods 0.000 description 17
- XLYOFNOQVPJJNP-UHFFFAOYSA-N water Substances O XLYOFNOQVPJJNP-UHFFFAOYSA-N 0.000 description 15
- ZCCIPPOKBCJFDN-UHFFFAOYSA-N calcium nitrate Chemical compound [Ca+2].[O-][N+]([O-])=O.[O-][N+]([O-])=O ZCCIPPOKBCJFDN-UHFFFAOYSA-N 0.000 description 12
- 239000002562 thickening agent Substances 0.000 description 12
- 239000011248 coating agent Substances 0.000 description 11
- PAWQVTBBRAZDMG-UHFFFAOYSA-N 2-(3-bromo-2-fluorophenyl)acetic acid Chemical compound OC(=O)CC1=CC=CC(Br)=C1F PAWQVTBBRAZDMG-UHFFFAOYSA-N 0.000 description 9
- 239000000126 substance Substances 0.000 description 9
- 239000003795 chemical substances by application Substances 0.000 description 7
- 239000007787 solid Substances 0.000 description 7
- 238000009736 wetting Methods 0.000 description 7
- LYCAIKOWRPUZTN-UHFFFAOYSA-N Ethylene glycol Chemical compound OCCO LYCAIKOWRPUZTN-UHFFFAOYSA-N 0.000 description 6
- 239000007864 aqueous solution Substances 0.000 description 6
- 230000000694 effects Effects 0.000 description 6
- 238000012360 testing method Methods 0.000 description 6
- 238000006243 chemical reaction Methods 0.000 description 5
- 239000000295 fuel oil Substances 0.000 description 5
- 239000004615 ingredient Substances 0.000 description 5
- 229910052751 metal Inorganic materials 0.000 description 5
- 239000002184 metal Substances 0.000 description 5
- WWZKQHOCKIZLMA-UHFFFAOYSA-N octanoic acid Chemical compound CCCCCCCC(O)=O WWZKQHOCKIZLMA-UHFFFAOYSA-N 0.000 description 5
- 235000021355 Stearic acid Nutrition 0.000 description 4
- 229940067232 ethanol 0.3 ml/ml medicated liquid soap Drugs 0.000 description 4
- 238000013508 migration Methods 0.000 description 4
- 230000005012 migration Effects 0.000 description 4
- QIQXTHQIDYTFRH-UHFFFAOYSA-N octadecanoic acid Chemical compound CCCCCCCCCCCCCCCCCC(O)=O QIQXTHQIDYTFRH-UHFFFAOYSA-N 0.000 description 4
- OQCDKBAXFALNLD-UHFFFAOYSA-N octadecanoic acid Natural products CCCCCCCC(C)CCCCCCCCC(O)=O OQCDKBAXFALNLD-UHFFFAOYSA-N 0.000 description 4
- 239000008117 stearic acid Substances 0.000 description 4
- 239000003784 tall oil Substances 0.000 description 4
- UMGDCJDMYOKAJW-UHFFFAOYSA-N thiourea Chemical compound NC(N)=S UMGDCJDMYOKAJW-UHFFFAOYSA-N 0.000 description 4
- QTBSBXVTEAMEQO-UHFFFAOYSA-N Acetic acid Chemical compound CC(O)=O QTBSBXVTEAMEQO-UHFFFAOYSA-N 0.000 description 3
- HEMHJVSKTPXQMS-UHFFFAOYSA-M Sodium hydroxide Chemical compound [OH-].[Na+] HEMHJVSKTPXQMS-UHFFFAOYSA-M 0.000 description 3
- 241000589634 Xanthomonas Species 0.000 description 3
- 238000004581 coalescence Methods 0.000 description 3
- 239000003026 cod liver oil Substances 0.000 description 3
- 238000000586 desensitisation Methods 0.000 description 3
- IPCSVZSSVZVIGE-UHFFFAOYSA-N hexadecanoic acid Chemical compound CCCCCCCCCCCCCCCC(O)=O IPCSVZSSVZVIGE-UHFFFAOYSA-N 0.000 description 3
- 238000010348 incorporation Methods 0.000 description 3
- 230000000977 initiatory effect Effects 0.000 description 3
- 230000014759 maintenance of location Effects 0.000 description 3
- 239000002923 metal particle Substances 0.000 description 3
- 239000003921 oil Substances 0.000 description 3
- 235000019198 oils Nutrition 0.000 description 3
- 230000002035 prolonged effect Effects 0.000 description 3
- 238000000926 separation method Methods 0.000 description 3
- 238000007711 solidification Methods 0.000 description 3
- 230000008023 solidification Effects 0.000 description 3
- 238000003860 storage Methods 0.000 description 3
- OMDQUFIYNPYJFM-XKDAHURESA-N (2r,3r,4s,5r,6s)-2-(hydroxymethyl)-6-[[(2r,3s,4r,5s,6r)-4,5,6-trihydroxy-3-[(2s,3s,4s,5s,6r)-3,4,5-trihydroxy-6-(hydroxymethyl)oxan-2-yl]oxyoxan-2-yl]methoxy]oxane-3,4,5-triol Chemical compound O[C@@H]1[C@@H](O)[C@@H](O)[C@@H](CO)O[C@@H]1OC[C@@H]1[C@@H](O[C@H]2[C@H]([C@@H](O)[C@H](O)[C@@H](CO)O2)O)[C@H](O)[C@H](O)[C@H](O)O1 OMDQUFIYNPYJFM-XKDAHURESA-N 0.000 description 2
- 239000004971 Cross linker Substances 0.000 description 2
- 229920000926 Galactomannan Polymers 0.000 description 2
- MHAJPDPJQMAIIY-UHFFFAOYSA-N Hydrogen peroxide Chemical compound OO MHAJPDPJQMAIIY-UHFFFAOYSA-N 0.000 description 2
- 229910002651 NO3 Inorganic materials 0.000 description 2
- NHNBFGGVMKEFGY-UHFFFAOYSA-N Nitrate Chemical compound [O-][N+]([O-])=O NHNBFGGVMKEFGY-UHFFFAOYSA-N 0.000 description 2
- 229920002472 Starch Polymers 0.000 description 2
- XSQUKJJJFZCRTK-UHFFFAOYSA-N Urea Natural products NC(N)=O XSQUKJJJFZCRTK-UHFFFAOYSA-N 0.000 description 2
- 239000002253 acid Substances 0.000 description 2
- 238000013019 agitation Methods 0.000 description 2
- 235000012716 cod liver oil Nutrition 0.000 description 2
- 239000000084 colloidal system Substances 0.000 description 2
- 238000002425 crystallisation Methods 0.000 description 2
- 230000008025 crystallization Effects 0.000 description 2
- 230000001419 dependent effect Effects 0.000 description 2
- 235000013312 flour Nutrition 0.000 description 2
- -1 i.e. Substances 0.000 description 2
- 238000011065 in-situ storage Methods 0.000 description 2
- 239000006193 liquid solution Substances 0.000 description 2
- 238000012986 modification Methods 0.000 description 2
- 230000004048 modification Effects 0.000 description 2
- KWYUFKZDYYNOTN-UHFFFAOYSA-M potassium hydroxide Inorganic materials [OH-].[K+] KWYUFKZDYYNOTN-UHFFFAOYSA-M 0.000 description 2
- 238000005204 segregation Methods 0.000 description 2
- 230000001235 sensitizing effect Effects 0.000 description 2
- 230000035939 shock Effects 0.000 description 2
- 235000019698 starch Nutrition 0.000 description 2
- HZTVIZREFBBQMG-UHFFFAOYSA-N 2-methyl-1,3,5-trinitrobenzene;[3-nitrooxy-2,2-bis(nitrooxymethyl)propyl] nitrate Chemical compound CC1=C([N+]([O-])=O)C=C([N+]([O-])=O)C=C1[N+]([O-])=O.[O-][N+](=O)OCC(CO[N+]([O-])=O)(CO[N+]([O-])=O)CO[N+]([O-])=O HZTVIZREFBBQMG-UHFFFAOYSA-N 0.000 description 1
- QTWJRLJHJPIABL-UHFFFAOYSA-N 2-methylphenol;3-methylphenol;4-methylphenol Chemical compound CC1=CC=C(O)C=C1.CC1=CC=CC(O)=C1.CC1=CC=CC=C1O QTWJRLJHJPIABL-UHFFFAOYSA-N 0.000 description 1
- VHUUQVKOLVNVRT-UHFFFAOYSA-N Ammonium hydroxide Chemical compound [NH4+].[OH-] VHUUQVKOLVNVRT-UHFFFAOYSA-N 0.000 description 1
- 241000894006 Bacteria Species 0.000 description 1
- OYPRJOBELJOOCE-UHFFFAOYSA-N Calcium Chemical compound [Ca] OYPRJOBELJOOCE-UHFFFAOYSA-N 0.000 description 1
- 239000004215 Carbon black (E152) Substances 0.000 description 1
- 229920002907 Guar gum Polymers 0.000 description 1
- DGAQECJNVWCQMB-PUAWFVPOSA-M Ilexoside XXIX Chemical compound C[C@@H]1CC[C@@]2(CC[C@@]3(C(=CC[C@H]4[C@]3(CC[C@@H]5[C@@]4(CC[C@@H](C5(C)C)OS(=O)(=O)[O-])C)C)[C@@H]2[C@]1(C)O)C)C(=O)O[C@H]6[C@@H]([C@H]([C@@H]([C@H](O6)CO)O)O)O.[Na+] DGAQECJNVWCQMB-PUAWFVPOSA-M 0.000 description 1
- OYHQOLUKZRVURQ-HZJYTTRNSA-N Linoleic acid Chemical compound CCCCC\C=C/C\C=C/CCCCCCCC(O)=O OYHQOLUKZRVURQ-HZJYTTRNSA-N 0.000 description 1
- 240000003183 Manihot esculenta Species 0.000 description 1
- 235000016735 Manihot esculenta subsp esculenta Nutrition 0.000 description 1
- GRYLNZFGIOXLOG-UHFFFAOYSA-N Nitric acid Chemical compound O[N+]([O-])=O GRYLNZFGIOXLOG-UHFFFAOYSA-N 0.000 description 1
- IOVCWXUNBOPUCH-UHFFFAOYSA-N Nitrous acid Chemical compound ON=O IOVCWXUNBOPUCH-UHFFFAOYSA-N 0.000 description 1
- 235000021314 Palmitic acid Nutrition 0.000 description 1
- DBMJMQXJHONAFJ-UHFFFAOYSA-M Sodium laurylsulphate Chemical class [Na+].CCCCCCCCCCCCOS([O-])(=O)=O DBMJMQXJHONAFJ-UHFFFAOYSA-M 0.000 description 1
- 150000007513 acids Chemical class 0.000 description 1
- 238000005273 aeration Methods 0.000 description 1
- 125000001931 aliphatic group Chemical group 0.000 description 1
- 150000001447 alkali salts Chemical class 0.000 description 1
- XFBXDGLHUSUNMG-UHFFFAOYSA-N alumane;hydrate Chemical compound O.[AlH3] XFBXDGLHUSUNMG-UHFFFAOYSA-N 0.000 description 1
- 239000000908 ammonium hydroxide Substances 0.000 description 1
- 239000003125 aqueous solvent Substances 0.000 description 1
- 229920001222 biopolymer Polymers 0.000 description 1
- 230000015572 biosynthetic process Effects 0.000 description 1
- 239000011575 calcium Substances 0.000 description 1
- 229910052791 calcium Inorganic materials 0.000 description 1
- 230000015556 catabolic process Effects 0.000 description 1
- 230000008859 change Effects 0.000 description 1
- 238000002485 combustion reaction Methods 0.000 description 1
- 230000006835 compression Effects 0.000 description 1
- 238000007906 compression Methods 0.000 description 1
- 238000004132 cross linking Methods 0.000 description 1
- 230000002939 deleterious effect Effects 0.000 description 1
- 238000001739 density measurement Methods 0.000 description 1
- 239000003975 dentin desensitizing agent Substances 0.000 description 1
- 230000003292 diminished effect Effects 0.000 description 1
- 238000004090 dissolution Methods 0.000 description 1
- 238000009826 distribution Methods 0.000 description 1
- 150000002148 esters Chemical class 0.000 description 1
- 238000004880 explosion Methods 0.000 description 1
- 150000002193 fatty amides Chemical class 0.000 description 1
- 230000005484 gravity Effects 0.000 description 1
- 239000000665 guar gum Substances 0.000 description 1
- 229960002154 guar gum Drugs 0.000 description 1
- 235000010417 guar gum Nutrition 0.000 description 1
- 230000035876 healing Effects 0.000 description 1
- 239000007970 homogeneous dispersion Substances 0.000 description 1
- 229930195733 hydrocarbon Natural products 0.000 description 1
- 150000002430 hydrocarbons Chemical class 0.000 description 1
- 229910052739 hydrogen Inorganic materials 0.000 description 1
- 239000012535 impurity Substances 0.000 description 1
- 239000003112 inhibitor Substances 0.000 description 1
- 239000003999 initiator Substances 0.000 description 1
- 230000001535 kindling effect Effects 0.000 description 1
- 238000002386 leaching Methods 0.000 description 1
- 235000020778 linoleic acid Nutrition 0.000 description 1
- OYHQOLUKZRVURQ-IXWMQOLASA-N linoleic acid Natural products CCCCC\C=C/C\C=C\CCCCCCCC(O)=O OYHQOLUKZRVURQ-IXWMQOLASA-N 0.000 description 1
- 238000012423 maintenance Methods 0.000 description 1
- 239000000463 material Substances 0.000 description 1
- 150000001455 metallic ions Chemical class 0.000 description 1
- 150000005217 methyl ethers Chemical class 0.000 description 1
- 238000005065 mining Methods 0.000 description 1
- 150000002763 monocarboxylic acids Chemical class 0.000 description 1
- WQEPLUUGTLDZJY-UHFFFAOYSA-N n-Pentadecanoic acid Natural products CCCCCCCCCCCCCCC(O)=O WQEPLUUGTLDZJY-UHFFFAOYSA-N 0.000 description 1
- 229910017604 nitric acid Inorganic materials 0.000 description 1
- 229960002446 octanoic acid Drugs 0.000 description 1
- 150000002889 oleic acids Chemical class 0.000 description 1
- 239000003973 paint Substances 0.000 description 1
- 239000004033 plastic Substances 0.000 description 1
- 229920001296 polysiloxane Polymers 0.000 description 1
- 230000002265 prevention Effects 0.000 description 1
- 238000005086 pumping Methods 0.000 description 1
- 230000001105 regulatory effect Effects 0.000 description 1
- 239000012266 salt solution Substances 0.000 description 1
- 235000008113 selfheal Nutrition 0.000 description 1
- 229910052708 sodium Inorganic materials 0.000 description 1
- 239000011734 sodium Substances 0.000 description 1
- 235000019333 sodium laurylsulphate Nutrition 0.000 description 1
- VWDWKYIASSYTQR-UHFFFAOYSA-N sodium nitrate Chemical class [Na+].[O-][N+]([O-])=O VWDWKYIASSYTQR-UHFFFAOYSA-N 0.000 description 1
- 235000010344 sodium nitrate Nutrition 0.000 description 1
- 239000003381 stabilizer Substances 0.000 description 1
- 230000008719 thickening Effects 0.000 description 1
- 235000013311 vegetables Nutrition 0.000 description 1
- 230000000007 visual effect Effects 0.000 description 1
Classifications
-
- 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
- C06B47/14—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 comprising a solid component and an aqueous phase
-
- C—CHEMISTRY; METALLURGY
- C06—EXPLOSIVES; MATCHES
- C06B—EXPLOSIVES OR THERMIC COMPOSITIONS; MANUFACTURE THEREOF; USE OF SINGLE SUBSTANCES AS EXPLOSIVES
- C06B23/00—Compositions characterised by non-explosive or non-thermic constituents
- C06B23/002—Sensitisers or density reducing agents, foam stabilisers, crystal habit modifiers
-
- C—CHEMISTRY; METALLURGY
- C06—EXPLOSIVES; MATCHES
- C06B—EXPLOSIVES OR THERMIC COMPOSITIONS; MANUFACTURE THEREOF; USE OF SINGLE SUBSTANCES AS EXPLOSIVES
- C06B23/00—Compositions characterised by non-explosive or non-thermic constituents
- C06B23/006—Stabilisers (e.g. thermal stabilisers)
Definitions
- An explosive blasting composition of the gel or slurry type which retains its sensitivity to detonation after being agitated or worked and method of making such composition are provided wherein a small amount of collector is added to the composition comprised of a stable dispersion of a metallic sensitizer and/or fuel particle throughout a thickened solution or fluid phase containing at least one inorganic oxidizer salt. The collector remains in solution throughout the fluid phase of the composition.
- the present invention relates to method of obtaining explosive blasting compositions of the gel or slurry type which retain their sensitivity to detonation after being agitated or worked, and to the resulting explosive compositions.
- it concerns the addition of a small amount of a collector to an explosive blasting composition comprised of a stable dispersion of metallic sensitizer and/or fuel particles throughout a thickened solution or fluid phase containing at least one inorganic oxidizer salt.
- the collector which is in solution throughout the fluid phase, prevents wetting of the surface of the metallic particles by the solution. Prevention of wetting allows explosive compositions to retain their sensitivity with working as will be more fully explained below.
- 3,249,474 discloses a method of regulating density and sensitivity of aqueous explosive blasting compositions whereby such coated fuel is used with an aqueous solution containing at least one dissolved inorganic oxidizer salt.
- a coated lyophobic metallic fuel in this manner, coupled with mechanical or chemical aeration or gassing, results in the inclusion of air or gas bubbles which adhere to the surface of the metal particles thereby forming an interface between the metal surface and the aqueous solvent. This adherence of included gas bubbles lowers the bulk density of the composition and provides for significantly enhanced sensitivity in comparison to similar compositions not containing lyophobic, coated, metallic fuel.
- Such hot spots can be sufficient in number and are high enough in temperature, owing to essentially adiabatic compression, to initiate rapid combustion or chemical reaction of the adjacent reactive material, i.e., oxidizer salt in solution and aluminum particles.
- oxidizer salt in solution and aluminum particles.
- This loosely termed hot spot theory is an explanation of the significant sensitizing effect that a small amount of very fine, coated lyophobic aluminum particles having a relatively high surface area (for increased entrapment of gas bubbles in addition to kindling effect) have been found to have in a fluid-phase-based explosive blasting composition.
- Empirical data coupled with direct density measurements and visual observation substantiate that lyophobic, coated metallic fuel particles vastly increase slurry or viscous liquid explosive composition sensitivity due to the incorporation of small gas or air bubbles into the composition which adhere to the surfaces of the particles.
- Gas bubbles are therefore preferably dispersed throughout an aqueous or fluid solution phase of a slurry explosive composition and can be formed either by chemical gassing or mechanical entrainment as is well known in the art.
- metallic fuel particles are admixed into a liquid oxidizer salt solution exposed to air or gas, particularly one which has been prethickened by thickeners such as galactomannan gums, starches, etc.
- thickeners such as galactomannan gums, starches, etc.
- small gas or air bubbles are entrained or incorporated into the solution phase. Further, such bubbles will be stably held in place in a viscous, prethickened solution.
- Chemical gassing agents such as decomposing hydrogen peroxide and alkali salts or nitrous acid, which agents can be present in the solution, comprise an in situ gassing means for explosive compositions.
- the present invention relates to explosive compositions which contain a fine dispersion of air or gas bubbles.
- composition sensitivity is greatly dependent upon adequate dispersion of the coated metallic particles containing attached gas bubbles throughout the aqueous or fluid phase, it is also greatly dependent upon the maintenance of these gas bubbles in this desired arrangement. It has been found that prolonged storage of explosive compositions containing finely dispersed gas bubbles, initially adhering to the surfaces of a coated metallic particle when first formed, has in some instances resulted in a loss of composition sensitivity and in many instances without a noticeable change in bulk density. Presumably, this phenomenon is a result of bubble separation from the metallic surface and possible subsequent migration and coalescence into larger, less sensitizing bubbles. Thus while 3 gas is still contained in the composition, the gas bubbles are no longer uniformly small and widely dispersed or in adherence to the metallic surfaces. Proper thickening and cross-linking of the fluid phase can, in most instances, prevent migration, coalescence and bubble separation to a significant degree.
- a onceformed composition of the coated, metallic fuel and/or sensitizer type is subsequently subjected to some type of agitation.
- packaged slurry or aqueous explosive composition is oftentimes compactly loaded into boreholes by tamping which results in a working or agitation of the composition.
- a once-formed composition may be subjected to repumping, or in other words, pumping after initial formation.
- a composition may be formulated and loaded into a container and then subsequently pumped or repumped from the container into a borehole or other receptacle. This repumping constitutes another example of working.
- this wetting phenomenon is that working results in a loss of the lyophobic coating (e.g. stearic acid, fatty acids, etc.) perhaps due to friction and consequential rubbing off" of the coating. Without this coating, the metallic surface is no longer lyophobic and becomes wetted by the liquid solution which displaces the adhering gas bubbles.
- the lyophobic coating e.g. stearic acid, fatty acids, etc.
- the collector used in the present invention may be similar to the coatings heretofore described in the above referenced patents.
- the collector can be any substance which will cause the flotation of a metallic, preferably aluminum, particle in the liquid menstrum of the explosive composition,
- the only essential requirement of the collector is that it remain in solution, i.e., be a miscible liquid in the explosive composition solution at temperatures of working of the explosive. Liquidity and miscibility are necessary in order that the collector can actively seek out metallic surfaces as they become exposed and thereby continually prevent their wetting as working continues.
- collectors of the present invention which have been found to be effective in various degrees in preventing loss of sensitivity are as follows: oleic, caprylic, linoleic and other fatty acids; red, tall and cod liver oils; green soap (vegetable oil-potassium hydroxide soap); Fels-naptha', xanthogen ester; sodium sulfated fatty amide derivatives; anionic sulphonates; and sodium lauryl sulfates,
- compositions of the present invention also contain, in solution and in addition, a collector which acts as an in situ, continuous coater or wetting inhibitor of the metal particles.
- the present invention has solved a problem which has been prevalent with the use of slurry or viscous liquid explosive compositions containing metallic fuel and/or sensitizer; that problem being loss of explosive sensitivity due to working. It has been discovered that the use of a collector in the liquid menstruum enables such compositions to retain their sensitivity upon working.
- frothers found effective for their conjunctive use with collector(s) are polypropylene glycol methyl ethers such as Dowfroth 250 and lOl2 which are represented by the following formula:
- a procedure for determining the relative effectiveness of a collector in preventing wetting of metallic particles was devised wherein two solutions, one containing water and the other containing dissolved ammonium nitrate (AN) were admixed with atomized aluminum particles and a collector and the degree of subsequent flotation of the particles in the solutions was observed.
- the atomized aluminum tested did not contain a preformed coating. ln this simplified test 200 ml of solution was placed in a 300 ml flask and 5 gms of atomized aluminum were added. Thereafter, each collector was added in an experimentally optimum amount which was about one-hundredth of the mass of the particles (0.05 gm) for the collectors tested (although each collector differed slightly).
- Flotation results are shown in Table I.
- green soap was found to be the best collector in AN containing solutions.
- Fels-Naptha was equivalent to green soap, but, when tested, it was not compatible with solutions containing calcium nitrate (CN).
- the fatty acids tested and reported in Table l were liquid at room temperatures (oleic, caprylic and linoleic).
- Other fatty acids with greater chain length such as capric, lauric, myristic, palmitic and stearic were found to work equally well at temperatures above their solidification temperatures even through they are solids at room temperature. The degree of flotation was substantially lessened when these longer-chained fatty acids were used in solutions having temperatures below their solidification temperatures.
- the optimum quantity of oleic acid is about one-hundredth the mass of the atomized aluminum for maximum flotation and is further roughly proportional to the surface area of the aluminum particles used.
- the fraction of flotation obtained as well as its stability was found to increase with increasing fineness of the atomized aluminum.
- the finest atomized aluminum tested had a particle size distribution such that 62% was 325 Tyler mesh. [t is possible that too fine of particles would not have sufficient surface for bubble contact; however, such an effect was not observed down to the particle size range tested.
- Hydrophilic colloid thickeners such as galactomannan gums, flours, starches, xanthomonas gums produced from the bacteria Xanthomonas campesrris, etc., are commonly used in aqueous slurry explosive compositions. Such thickeners render the aqueous solution viscous thereby preventing segregation of dispersed solid ingredients such as metallic fuels and/or sensitizers, undissolved oxidiizer salts. carbonaceous fuels, etc., as well as preventing migration and coalescence of finely dispersed gas bubbles. Such thickeners also provide water resistance to the compositions to prevent breakdown of the compositions and leaching of oxidizer salts in the presence of water.
- thickeners are almost essential for stability, homogeneity and water resistance of aqueous gel or slurry type explosive blasting compositions.
- thickeners can be cross-linked by cross-linkers such as metallic ions.
- Slurry explosive cross-linkers and thickeners are widely used and common in the art.
- Thickeners are essential to compositions of the present invention particularly for preventing metallic particle segregation and gas bubble migration.
- atomized aluminum was found to have good flotation characteristics in water thickened with small quantities (concentrations were just below the values at which the viscosity of the solution would significantly interfere with particulate mobility and thus degree of flotation) of Brazilian tapioca flour, guar gum derivative of low molecular weight (Stein-Hall L808) and xanthomonas gum (General Mills XB23) and containing oleic acid as a collector.
- Other collectors were found to be similarly compatible with hydrophilic colloid thickeners.
- Table ll summarizes test results obtained for slurry or gel type explosive blasting compositions using various collector/frother combinations. All percentages refer to weight percent based on the total composition.
- the CN refers to Norsk Hyro calcium nitrate which is a commercial grade CN consisting of about 80% CN, about 15% water (as water of crystallization) and about AN.
- the thickener was General Mills XB-23, a biopolymer gum produced from the bacteria Xanthonomonas campestris.
- compositions of Table II were prepared by first dissolving the oxidizer salt(s) in an aqueous solution containing water, liquid fuels (if any), thiourea as a nitrate gassing agent accelerator (if used), the thickening agent, a collector or combination of collectors, and frother (if used). Such dissolution was accomplished at a temperature preferably of about at least C higher than the fudge point or crystallization temperature of the solution. Thereafter, the remaining solid ingredients were added to the thickened solution (i.e., aluminum, gilsonite, ground AN) along with the nitrate gassing agent. The composition was subsequently mixed to provide a uniform, homogeneous dispersion of solid ingredients throughout an aqueous fluid phase.
- the detonation results of Table II indicate the minimum booster required to detonate a 2-inch diameter explosive charge at 5C.
- the symbol F stands for failure of the charge to detonate and Det" stands for effective charge detonation.
- the No.” 5, 6, etc. stands for the size of a standard commercial blasting cap used as the booster with the larger the number corresponding to the greater the cap boostering power.
- a number such as 5" followed by a g" represents that the charge would not detonate with a regular cap and thus stands for the amount of grams of a pentolite booster required for detonation.
- Minimum booster required for detonation is a direct measure of an explosive compositions relative sensitivity. The smaller the booster. the more sensitive the composition.
- compositions were tested for relative sensitivity both before and after working.
- Working was accomplished by repumping an explosive composition through a Model H724 Viking pump at a rate of 80 pounds per minute. A 40-pound sample of slurry was used and thus was cycled through the pump two times per minute.
- a comparison of the detonation results of mixes A. B and C shows that oleic acid as a collector has little effect on sensitivity of a composition which has not been worked or repumped, but greatly enhances the sensitivity of a composition which has been worked relative to a composition not containing the collector.
- a comparison of the results of mixes E and F shows that when a frother is used with an oleic acid collector, the sensitivity of the composition after repumping or working is greater than if the frother is not used.
- a comparison of the results of mixes G and H shows that when fuel oil is used with oleic acid the sensitivity of the composition after working is greater than if the fuel oil is not, used.
- the results for mixes H and l surprisingly show that sensitivity is even increased upon working. Fiyrthermore, it is also greatly significant, as evident from the results of mixes H and I, that aqueous explosive composition sensitivity may be obtained at higher than nonnal slurry densities due to the control of bubble size and location by the use of frothers and collectors.
- a soap was used as a collector which increased the compositions sensitivity upon working. Such result is significant since soaps have been generally regarded as desensitizing agents for slurries sensitized by paint grade aluminum.
- the explosive compositions of the present invention are designed to retain their sensitivity after being subjected to working. They are also capable of stability over prolonged storage due in some respect to the ability of a collector to maintain adherence of fine gas bubbles to the surfaces of metallic fuels and/or sensitizers.
- the explosive compositions of the invention may, if desired, be used, i.e., detonated, immediately after being placed into a borehole, they also remain stable and this may be detonated even after encountering water in the borehole and/or being allowed to re main in the borehole for many days.
- compositions may also be packaged in any suitable container, for example, plastic bags or cardboard tubes, and thereafter detonated in either vertical or horizontal boreholes or any other desired location.
- frother is selected from the group which consists of polypropylene glycol methyl ether and silicone resin.
- an explosive composition comprising a thickened solution phase of at least one oxidizing salt and coated (stearic acid) atomized aluminum and a rating of 5 indicates no flotation.
- mfitanic part cles as fue an sensitizer dispersed throughout the solution phase the improvement com- Table ll AN 27.
- a method for preventing the loss of sensitivity of a gas-containing blasting composition upon being worked which composition comprises a continuous thickened solution phase having dissolved therein at least one inorganic oxidizer salt and metallic particles as fuel and/or sensitizer dispersed throughout the solution phase which method includes incorporating into the solution phase a small amount of a miscible, liquid collector, which is capable of causing floatation of the metallic particles in the solution phase when such phase is not thickened and which retains its liquidity and miscibility at intended temperatures of working.
- a method according to claim 1 which includes the additional step of adding a frother to the fluid phase to stabilize and control bubble size.
- a miscible, liquid collector which is capable of causing flotation of the metallic particles in the solution phase when such solution phase is not thickened and which retains its liquidity and miscibility at intended temperatures of working, to prevent the metallic particles from becoming wetted upon working thereby causing the composition to lose its sensitivity.
- composition according to claim 8 wherein the collector is a fatty acid.
- composition according to claim 9 wherein the fatty acid is oleic acid.
- a composition according to claim 8 containing, in addition. a small amount of a frother to stabilize and control bubble size.
- a composition according to claim 11 wherein the frother is selected from the group which consists of polypropylene glycol methyl ether and silicone resin.
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Abstract
An explosive blasting composition of the gel or slurry type which retains its sensitivity to detonation after being agitated or worked and method of making such composition are provided wherein a small amount of collector is added to the composition comprised of a stable dispersion of a metallic sensitizer and/or fuel particle throughout a thickened solution or fluid phase containing at least one inorganic oxidizer salt. The collector remains in solution throughout the fluid phase of the composition.
Description
United States Patent [191 Cook et al.
[54] EXPLOSIVE COMPOSITIONS CONTAINING METALLIC FUEL PARTICLES AND METHOD OF PREPARATION THEREOF [75] inventors: Melvin A. Cook, Salt Lake City;
Mark J. I-lagmann, Summit Park, both of Utah [73] Assignee: Ireco Chemicals, Salt Lake City,
Utah
[22] Filed: Feb. 21, 1974 [21] Appl. No.: 444,691
[52] US. Cl. 149/44; 149/41; 149/43; 149/61; 149/46; 149/60 [51] Int. Cl. C0613 33/02 [58] Field of Search 149/44, 41, 43, 46, 60, 149/61 [56] References Cited UNITED STATES PATENTS 3,711,345 l/l973 Tomic 149/44 X Dec. 16, 1975 Tomic 149/44 X Tomic 149/44 X 57 1 ABSTRACT An explosive blasting composition of the gel or slurry type which retains its sensitivity to detonation after being agitated or worked and method of making such composition are provided wherein a small amount of collector is added to the composition comprised of a stable dispersion of a metallic sensitizer and/or fuel particle throughout a thickened solution or fluid phase containing at least one inorganic oxidizer salt. The collector remains in solution throughout the fluid phase of the composition.
12 Claims, No Drawings EXPLOSIVE COMPOSITIONS CONTAINING METALLIC FUEL PARTICLES AND METHOD OF PREPARATION THEREOF The present invention relates to method of obtaining explosive blasting compositions of the gel or slurry type which retain their sensitivity to detonation after being agitated or worked, and to the resulting explosive compositions. Particularly, it concerns the addition of a small amount of a collector to an explosive blasting composition comprised of a stable dispersion of metallic sensitizer and/or fuel particles throughout a thickened solution or fluid phase containing at least one inorganic oxidizer salt. The collector, which is in solution throughout the fluid phase, prevents wetting of the surface of the metallic particles by the solution. Prevention of wetting allows explosive compositions to retain their sensitivity with working as will be more fully explained below.
The use of metallic, notably aluminum, particles in explosive compositions or blasting agents of the viscous liquid gel or slurry type containing a thickened solution of at least one inorganic oxidizer salt and solid and/or liquid fuel has been common throughout the past or years with the advent of commonly termed slurry explosives." US. Pat. No. 3,297,502 discloses slurry explosives or aqueous blasting agents comprising water and inorganic oxidizer salts and containing metallic fuel such as aluminum particles having a preformed coating. The aluminum particles disclosed in this patent function as fuel and have a preformed coating composed of a liquid oil and a monocarboxylic aliphatic acid. The coating is employed to prevent an aluminum-water reaction which evolves gas and liberates heat and thus can render an explosive dangerous for storage and handling.
In addition to preventing unwanted reaction of the metal with solution, coating metallic fuel particles prior to their incorporation into an aqueous solution of an explosive composition has also been found to provide other advantageous results. US. Pat. No. 3,249,474 discloses the use of aluminum particles having a preformed coating such as stearic acid that renders the aluminum surface lyophobic and thus repellant to the liquid component of the explosive composition. The coatings disclosed in US. Pat No. 3,249,474 are similar to those disclosed in US. Pat. No. 3,297,502. US. Pat. No. 3,249,474 discloses a method of regulating density and sensitivity of aqueous explosive blasting compositions whereby such coated fuel is used with an aqueous solution containing at least one dissolved inorganic oxidizer salt. As this patent describes, it was found that the incorporation of a coated lyophobic metallic fuel in this manner, coupled with mechanical or chemical aeration or gassing, results in the inclusion of air or gas bubbles which adhere to the surface of the metal particles thereby forming an interface between the metal surface and the aqueous solvent. This adherence of included gas bubbles lowers the bulk density of the composition and provides for significantly enhanced sensitivity in comparison to similar compositions not containing lyophobic, coated, metallic fuel.
Apparently, and as suggested in US. Pat. No. 3,249,474, the inclusion of gas bubbles and their adherence to the surfaces of lyophobic metallic particles in explosive compositions creates numerous, small voids or gas pockets which are compressible upon initiation or detonation of the composition. When a detonation initiation shock wave caused by an initiator such as a blasting cap or booster travels through such a composition, apparently the resulting localized and extremely high pressure of the wave compresses these numerous gas pockets causing the gas entrapped therein to obtain an extremely high temperature. Such hot spots" thus created can be sufficient in number and are high enough in temperature, owing to essentially adiabatic compression, to initiate rapid combustion or chemical reaction of the adjacent reactive material, i.e., oxidizer salt in solution and aluminum particles. When a sufficient number of such hot spots are simultaneously created, and due to the ability of a continuous fluid phase to transmit the detonation initiation shock wave at high velocity, a powerful explosion ensues. This loosely termed hot spot theory is an explanation of the significant sensitizing effect that a small amount of very fine, coated lyophobic aluminum particles having a relatively high surface area (for increased entrapment of gas bubbles in addition to kindling effect) have been found to have in a fluid-phase-based explosive blasting composition. Empirical data coupled with direct density measurements and visual observation substantiate that lyophobic, coated metallic fuel particles vastly increase slurry or viscous liquid explosive composition sensitivity due to the incorporation of small gas or air bubbles into the composition which adhere to the surfaces of the particles.
Gas bubbles are therefore preferably dispersed throughout an aqueous or fluid solution phase of a slurry explosive composition and can be formed either by chemical gassing or mechanical entrainment as is well known in the art. As indicated above, when metallic fuel particles are admixed into a liquid oxidizer salt solution exposed to air or gas, particularly one which has been prethickened by thickeners such as galactomannan gums, starches, etc., small gas or air bubbles are entrained or incorporated into the solution phase. Further, such bubbles will be stably held in place in a viscous, prethickened solution. Chemical gassing agents such as decomposing hydrogen peroxide and alkali salts or nitrous acid, which agents can be present in the solution, comprise an in situ gassing means for explosive compositions. A substantial proportion of bubbles formed either mechanically and/or chemically adhere to the surface of dispersed lyophobic metallic particles which can be considered somewhat as bubble attachment or collection centers. The smaller the bubble, theoretically, the better it functions as a reaction site or hot spot. The present invention relates to explosive compositions which contain a fine dispersion of air or gas bubbles.
Since composition sensitivity is greatly dependent upon adequate dispersion of the coated metallic particles containing attached gas bubbles throughout the aqueous or fluid phase, it is also greatly dependent upon the maintenance of these gas bubbles in this desired arrangement. It has been found that prolonged storage of explosive compositions containing finely dispersed gas bubbles, initially adhering to the surfaces of a coated metallic particle when first formed, has in some instances resulted in a loss of composition sensitivity and in many instances without a noticeable change in bulk density. Presumably, this phenomenon is a result of bubble separation from the metallic surface and possible subsequent migration and coalescence into larger, less sensitizing bubbles. Thus while 3 gas is still contained in the composition, the gas bubbles are no longer uniformly small and widely dispersed or in adherence to the metallic surfaces. Proper thickening and cross-linking of the fluid phase can, in most instances, prevent migration, coalescence and bubble separation to a significant degree.
An ever more deleterious phenomenon concerning loss or lowering of explosive composition sensitivity is observed when a onceformed composition of the coated, metallic fuel and/or sensitizer type is subsequently subjected to some type of agitation. For example, packaged slurry or aqueous explosive composition is oftentimes compactly loaded into boreholes by tamping which results in a working or agitation of the composition. Furthermore, a once-formed composition may be subjected to repumping, or in other words, pumping after initial formation. For instance, a composition may be formulated and loaded into a container and then subsequently pumped or repumped from the container into a borehole or other receptacle. This repumping constitutes another example of working.
Working is observed to result in significant desensitization of a composition containing fine, coated lyophobic metallic particles dispersed throughout an aerated or gassified fluid phase having dissolved therein at least one inorganic oxidizer salt. Apparently, such working results in a separation of the gas bubbles from the coated metallic surfaces, which results in loss of potential hot spots adjacent to the metallic fuel. In effect, the metallic surface becomes wetted," i.e., the liquid solution is in direct contact with the metal surface and is therefore not separated therefrom by an interfacing air or gas bubble. Therefore, wetting of the metallic surface results in a direct loss of explosive sensitivity.
A possible explanation of this wetting phenomenon is that working results in a loss of the lyophobic coating (e.g. stearic acid, fatty acids, etc.) perhaps due to friction and consequential rubbing off" of the coating. Without this coating, the metallic surface is no longer lyophobic and becomes wetted by the liquid solution which displaces the adhering gas bubbles.
It has now been discovered that loss of sensitivity from working of such explosive compositions containing coated metallic fuel and/or sensitizer particles can be prevented by providing, in solution, a liquid collector which is capable of flotation of metallic particles in a liquid menstruum. As will be shown in the examples below, a collector in solution results in compositions which after being worked will retain their sensitivity to a significantly greater extent than compositions not containing such an ingredient.
A possible explanation of the observed effect of the collector on sensitivity, which corresponds to that given for the desensitization upon working phenomenon described above, is that the collector in solution is free to actively seek out and adhere to exposed metallic surfaces which have lost their lyophobic coating due to working. Thus, liquid collectors in solution allow self healing" of exposed surfaces whereas solid or preformed coatings will not self-heal. Thus collectors allow such surfaces to retain their lyophobic nature thereby affording their retention of adhering, interfacing gas bubbles and thus retention of sensitivity.
The collector used in the present invention may be similar to the coatings heretofore described in the above referenced patents. However, the collector can be any substance which will cause the flotation of a metallic, preferably aluminum, particle in the liquid menstrum of the explosive composition, The only essential requirement of the collector is that it remain in solution, i.e., be a miscible liquid in the explosive composition solution at temperatures of working of the explosive. Liquidity and miscibility are necessary in order that the collector can actively seek out metallic surfaces as they become exposed and thereby continually prevent their wetting as working continues. Examples of collectors of the present invention which have been found to be effective in various degrees in preventing loss of sensitivity are as follows: oleic, caprylic, linoleic and other fatty acids; red, tall and cod liver oils; green soap (vegetable oil-potassium hydroxide soap); Fels-naptha', xanthogen ester; sodium sulfated fatty amide derivatives; anionic sulphonates; and sodium lauryl sulfates,
Some of the above collectors have been used heretofore as coatings for the metallic particle surfaces in explosive compositions. For instance, U.S. Pat. No. 3,297,502 discussed previously discloses the use of fatty acids including oleic acid as coatings that are particularly effective if used in conjunction with a liquid hydrocarbon oil such as fuel oil. As mentioned, this patent describes preforming such coating on the metal prior to the particles introduction into the liquid menstruum. U.S. Pat. No. 3,249,474 discussed previously discloses the use of normally solid fatty acids such as stearic acid, palmitic acid, etc., among others as preformed lyophobic coatings to render the surfaces of the metal particles lyophobic. As discussed above, neither of these references disclose a means whereby desensiti zation due to working can be prevented. The present invention distinguishes from the disclosure in these two patents in that while preformed coated metal is preferably used in the compositions of the present invention, the compositions also contain, in solution and in addition, a collector which acts as an in situ, continuous coater or wetting inhibitor of the metal particles.
Thus the present invention has solved a problem which has been prevalent with the use of slurry or viscous liquid explosive compositions containing metallic fuel and/or sensitizer; that problem being loss of explosive sensitivity due to working. It has been discovered that the use of a collector in the liquid menstruum enables such compositions to retain their sensitivity upon working.
It also has been found in the present invention that the use of a frothing agent or frother as a gas bubble stabilizer in conjunction with the use of a collector allows for even increased composition sensitivity retention upon working. Frothers which limit bubble size and increase their stability afford this added effectiveness, Examples of frothers found effective for their conjunctive use with collector(s) are polypropylene glycol methyl ethers such as Dowfroth 250 and lOl2 which are represented by the following formula:
CH,, (0 C,H,),-oH and which have an average molecular weight range of from about 200 to about 400. The Dowfroth frothers are further described in the booklet, Flotation Fundamentals and Mining Chemicals, The Dow Chemical Company, 1970. Another frother found effective is silicone resin having a specific gravity at 25C of L06 [.08 and a viscosity at 25C of 1,200 2,000 centistokes. This silicone resin is known commercially as Union Carbide R-23 and is further described in a Product Information Bulletin on Union Carbide R-23, R-230 and RE-23l Silicone Water Repellants. All of the above three frothers appeared to reduce bubble size and increase bubble stability of all bubbles in a thickened liquid menstruum including those attached to and those separate from metallic particles. Moreover, all three frothers were found to increase both the stability and degree of flotation of aluminum particles in a liquid menstrum when used with a fatty acid collector such as oleic acid. Monocarboxylic acid collectors, i.e., oleic, caprylic, etc., have some inherent frother characteristics which enhances their use as collectors.
A procedure for determining the relative effectiveness of a collector in preventing wetting of metallic particles was devised wherein two solutions, one containing water and the other containing dissolved ammonium nitrate (AN) were admixed with atomized aluminum particles and a collector and the degree of subsequent flotation of the particles in the solutions was observed. The atomized aluminum tested did not contain a preformed coating. ln this simplified test 200 ml of solution was placed in a 300 ml flask and 5 gms of atomized aluminum were added. Thereafter, each collector was added in an experimentally optimum amount which was about one-hundredth of the mass of the particles (0.05 gm) for the collectors tested (although each collector differed slightly). Soaps, however, were found to also be effective at a much lower concentration. After addition of the collector, the flask was stoppered and given ten hard vertical shakes. The subsequent degree of flotation of the atomized aluminum was then observed. As a standard reference point, oleic acid was found to provide 90% of all aluminum particles floated on top of the solution due to adhering gas bubbles and of the particles fell to the bottom of the flask) in a 50/50 by weight ANIH- O solution. When a collector was not used, no flotation (0%) was observed. A Hallimond-Ewers flotation cell was also used in similar testing, but it tended to over-rate the effectiveness of the collectors since it would not distinguish between momentary (an order of a second) and prolonged (an order of several seconds or longer) flotation.
Flotation results are shown in Table I. As is readily apparent from Table I, green soap was found to be the best collector in AN containing solutions. Fels-Naptha was equivalent to green soap, but, when tested, it was not compatible with solutions containing calcium nitrate (CN). The fatty acids tested and reported in Table l were liquid at room temperatures (oleic, caprylic and linoleic). Other fatty acids with greater chain length such as capric, lauric, myristic, palmitic and stearic were found to work equally well at temperatures above their solidification temperatures even through they are solids at room temperature. The degree of flotation was substantially lessened when these longer-chained fatty acids were used in solutions having temperatures below their solidification temperatures. These latter acids are therefore applicable for use as collectors in the present invention only if the explosive compositions are worked at temperatures above their respective solidification temperatures. Short chain length fatty acids such as caproic, valeric, butyric, isobutyric and propionic caused no noticeable flotation presumably because they are not sufficiently water repellant. Red oil (crude oleic acid), tall oil and cod liver oil were found to have flotation characteristics equivalent to oleic acid.
It was also found that the optimum quantity of oleic acid is about one-hundredth the mass of the atomized aluminum for maximum flotation and is further roughly proportional to the surface area of the aluminum particles used. The fraction of flotation obtained as well as its stability was found to increase with increasing fineness of the atomized aluminum. The finest atomized aluminum tested had a particle size distribution such that 62% was 325 Tyler mesh. [t is possible that too fine of particles would not have sufficient surface for bubble contact; however, such an effect was not observed down to the particle size range tested.
A series of tests was accomplished to determine the effect of pH on flotation of atomized aluminum in water containing tall oil as the collector. Maximum flotation was found in the pH range of from 4 to 6 but was only slightly diminished over the pH range of from 3 to 7. Dilute nitric acid and ammonium hydroxide or acetic acid and sodium hydroxide were used for adjusting the pH. All other collectors tested were found to perform similarly in this pH range of from 3 to 7.
Hydrophilic colloid thickeners such as galactomannan gums, flours, starches, xanthomonas gums produced from the bacteria Xanthomonas campesrris, etc., are commonly used in aqueous slurry explosive compositions. Such thickeners render the aqueous solution viscous thereby preventing segregation of dispersed solid ingredients such as metallic fuels and/or sensitizers, undissolved oxidiizer salts. carbonaceous fuels, etc., as well as preventing migration and coalescence of finely dispersed gas bubbles. Such thickeners also provide water resistance to the compositions to prevent breakdown of the compositions and leaching of oxidizer salts in the presence of water. In general, thickeners are almost essential for stability, homogeneity and water resistance of aqueous gel or slurry type explosive blasting compositions. For added stability thickeners can be cross-linked by cross-linkers such as metallic ions. Slurry explosive cross-linkers and thickeners are widely used and common in the art.
Thickeners are essential to compositions of the present invention particularly for preventing metallic particle segregation and gas bubble migration. Thus a series of tests was made in which atomized aluminum was found to have good flotation characteristics in water thickened with small quantities (concentrations were just below the values at which the viscosity of the solution would significantly interfere with particulate mobility and thus degree of flotation) of Brazilian tapioca flour, guar gum derivative of low molecular weight (Stein-Hall L808) and xanthomonas gum (General Mills XB23) and containing oleic acid as a collector. Other collectors were found to be similarly compatible with hydrophilic colloid thickeners.
When the collectors were tested for flotation of atomized aluminum in aqueous ammonium nitrate solutions it was found that a fraction of each of oleic, caprylic and linoleic acid and red, tall and cod liver oil formed a white insoluble product although good flotation was still observed. A similar product was not observed with solutions containing calcium and sodium nitrates. The white insoluble product is attributed to a reaction between the ammonium radical and the by droxy fatty acid component present as an impurity in the collectors.
Combinations of different collectors and combinations of collectors with other ingredients were found to provide particularly good flotation. Fuel oil did not by itself cause flotation, but. when combined with oleic acid as the collector in solution, flotation was enhanced over that obtained by oleic acid separately. This same effect was observed with ethylene glycol. A combination of green soap and oleic acid was found to cause better flotation than that obtained by either separately. Higher order combinations such as oleic acid, fuel oil. ethylene glycol and frother were also found to be very effective.
Table ll summarizes test results obtained for slurry or gel type explosive blasting compositions using various collector/frother combinations. All percentages refer to weight percent based on the total composition. The CN refers to Norsk Hyro calcium nitrate which is a commercial grade CN consisting of about 80% CN, about 15% water (as water of crystallization) and about AN. The thickener was General Mills XB-23, a biopolymer gum produced from the bacteria Xanthonomonas campestris.
The compositions of Table II were prepared by first dissolving the oxidizer salt(s) in an aqueous solution containing water, liquid fuels (if any), thiourea as a nitrate gassing agent accelerator (if used), the thickening agent, a collector or combination of collectors, and frother (if used). Such dissolution was accomplished at a temperature preferably of about at least C higher than the fudge point or crystallization temperature of the solution. Thereafter, the remaining solid ingredients were added to the thickened solution (i.e., aluminum, gilsonite, ground AN) along with the nitrate gassing agent. The composition was subsequently mixed to provide a uniform, homogeneous dispersion of solid ingredients throughout an aqueous fluid phase.
The detonation results of Table II indicate the minimum booster required to detonate a 2-inch diameter explosive charge at 5C. The symbol F" stands for failure of the charge to detonate and Det" stands for effective charge detonation. The No." 5, 6, etc., stands for the size of a standard commercial blasting cap used as the booster with the larger the number corresponding to the greater the cap boostering power. A number such as 5" followed by a g" represents that the charge would not detonate with a regular cap and thus stands for the amount of grams of a pentolite booster required for detonation. Minimum booster required for detonation is a direct measure of an explosive compositions relative sensitivity. The smaller the booster. the more sensitive the composition.
As shown in the table, the compositions were tested for relative sensitivity both before and after working. Working was accomplished by repumping an explosive composition through a Model H724 Viking pump at a rate of 80 pounds per minute. A 40-pound sample of slurry was used and thus was cycled through the pump two times per minute. A comparison of the detonation results of mixes A. B and C shows that oleic acid as a collector has little effect on sensitivity of a composition which has not been worked or repumped, but greatly enhances the sensitivity of a composition which has been worked relative to a composition not containing the collector. A comparison of the results of mixes E and F shows that when a frother is used with an oleic acid collector, the sensitivity of the composition after repumping or working is greater than if the frother is not used. A comparison of the results of mixes G and H shows that when fuel oil is used with oleic acid the sensitivity of the composition after working is greater than if the fuel oil is not, used. In fact. the results for mixes H and l surprisingly, show that sensitivity is even increased upon working. Fiyrthermore, it is also greatly significant, as evident from the results of mixes H and I, that aqueous explosive composition sensitivity may be obtained at higher than nonnal slurry densities due to the control of bubble size and location by the use of frothers and collectors.
In example I, a soap was used as a collector which increased the compositions sensitivity upon working. Such result is significant since soaps have been generally regarded as desensitizing agents for slurries sensitized by paint grade aluminum.
All of the results shown in Table ll are consistent with the results shown in Table l as well as the results of various flotation tests described previously.
The explosive compositions of the present invention are designed to retain their sensitivity after being subjected to working. They are also capable of stability over prolonged storage due in some respect to the ability of a collector to maintain adherence of fine gas bubbles to the surfaces of metallic fuels and/or sensitizers.
While the explosive compositions of the invention may, if desired, be used, i.e., detonated, immediately after being placed into a borehole, they also remain stable and this may be detonated even after encountering water in the borehole and/or being allowed to re main in the borehole for many days.
In addition to being used unpackaged, e.g., in large diameter borehole blasting operations, the compositions may also be packaged in any suitable container, for example, plastic bags or cardboard tubes, and thereafter detonated in either vertical or horizontal boreholes or any other desired location.
While the present invention has been described with reference to certain illustrative examples and preferred embodiments, various modifications will be apparent to those skilled in the art and any such modifications are intended to be within the scope of the invention as set forth in the appended claims.
Table l Flotation of Atomized Aluminum With Various Collectors [Listed by descriptive name [brand chemical or both] and commercial manufacturer in some instances) Flotation Rating Aqueous Solution Containing AN Water [did-- Table l-continued Flotation of Atomized Aluminum With Various Collectors (Listed by descriptive name lbrand. chemical or bothl and commercial manufacturer in some instances) Flotation Rating* Aqueous Solution Water Containing AN Cresylic acid 2 S A ralmg of l indicates flotation superior to that obtained with commercially 5. A method according to claim 1 wherein the collector is a soap.
6. A method according to claim 2 wherein the frother is selected from the group which consists of polypropylene glycol methyl ether and silicone resin.
7. A method according to claim 1 wherein the metallic particles are aluminum.
8. In an explosive composition comprising a thickened solution phase of at least one oxidizing salt and coated (stearic acid) atomized aluminum and a rating of 5 indicates no flotation. mfitanic part cles as fue an sensitizer dispersed throughout the solution phase the improvement com- Table ll AN 27. l SN H O Thiourea Thickener No.6 Det No.5 F. No.5 F. No.5 F.
1.23 35g Det 1.08 l60g F.
1.19 35g Det g F. 5g F.
l .20 5g Det 1.16 5g Det No.8 F. No.3 F.
Mix F used Union Carbide R-23. mixes G and H used Dow DFF-4082.
What is claimed is:
l. A method for preventing the loss of sensitivity of a gas-containing blasting composition upon being worked which composition comprises a continuous thickened solution phase having dissolved therein at least one inorganic oxidizer salt and metallic particles as fuel and/or sensitizer dispersed throughout the solution phase which method includes incorporating into the solution phase a small amount of a miscible, liquid collector, which is capable of causing floatation of the metallic particles in the solution phase when such phase is not thickened and which retains its liquidity and miscibility at intended temperatures of working.
2. A method according to claim 1 which includes the additional step of adding a frother to the fluid phase to stabilize and control bubble size.
3. A method according to claim 1 wherein the collector is a fatty acid.
4. A method according to claim 3 wherein the fatty acid is oleic acid.
No.6 Det No.6 Det 5g Det No.8 F.
1.45 l60g F.
1.45 l60g Det 1.22 L23 No.6 Det No.6 Del No.5 F. No.5 F. g F.
1.34 No.8 Det 1.35 No.8 Det 1.37 lg F.
l .20 5g Det No.8 F.
[.36 353 Det L40 35g Det 1.17 loOg F.
LlU
prising, in the solution phase, a small amount of a miscible, liquid collector. which is capable of causing flotation of the metallic particles in the solution phase when such solution phase is not thickened and which retains its liquidity and miscibility at intended temperatures of working, to prevent the metallic particles from becoming wetted upon working thereby causing the composition to lose its sensitivity.
9. A composition according to claim 8 wherein the collector is a fatty acid.
10. A composition according to claim 9 wherein the fatty acid is oleic acid.
11. A composition according to claim 8 containing, in addition. a small amount of a frother to stabilize and control bubble size.
12. A composition according to claim 11 wherein the frother is selected from the group which consists of polypropylene glycol methyl ether and silicone resin.
Claims (12)
1. A METHOD FOR PREVENTING THE LOSS OF SENSITIVITY OF A GASCONTAINING BLASTING COMPOSITION UPON BEING WORKED WHICH COMPOSITION COMPRISES A CONTINUOUS THICKENED SOLUTION PHASE HAVING DISSOLVED THEREIN AT LEAST ONE INORGANIC OXIDIZER SALT AND METALLIC PARTICLES AS FUEL AND/OR SENSITIZER DISPERSED THROUGHOUT THE SOLUTION PHASE WHICH METHOD INCLUDES INCORPORATING INTO THE SOLUTION PHASE A SMALL AMOUNT OF A MISCIBLE, LIQUID COLLECTOR, WHICH IS CAPABLE OF CAUSING FLOATATION OF THE METALLIC PARTICLES IN THE SOLUTION PHASE WHEN SUCH PHASE IS NOT THICKENED AND WHICH EETAINS ITS LIQUIDITY AND MISCIBILITY AT INTENDED TEMPERATURES OF WORKING.
2. A method according to claim 1 which includes the additional step of adding a frother to the fluid phase to stabilize and control bubble size.
3. A method according to claim 1 wherein the collector is a fatty acid.
4. A method according to claim 3 wherein the fatty acid is oleic acid.
5. A method according to claim 1 wherein the collector is a soap.
6. A method according to claim 2 wherein the frother is selected from the group which consists of polypropylene glycol methyl ether and silicone resin.
7. A method according to claim 1 wherein the metallic particles are aluminum.
8. IN AN EXPLOSIVE COMPOSITION COMPRISING A THICKNEED SOLUTION PHASE OF AT LEAST ONE OXIDIZING SALT AND METALLIC PARTICLES AS FUEL AND/OR SENSITIZER DISPERSED THROUGHOUT THE SOLUTION PHASE THE IMPROVEMENT COMPRISING, IN THE SOLUTION PHASE, A SMALL AMOUNT OF A MISCIBLE,LIQUID COLLECTOR, WHICH IS CAPABLE OF CAUSING FLOTATION OF THE METALLIC PARTICLES IN THE SOLUTION PHASE WHEN SUCH SOLUTION PHASE IS NOT THICKENED AND WHICH RETAINS ITS LIQUIDITY AND MISCIBILITY AAT INTENDED TEMPERATURES OF WORKING, TO PREVENT THE METALLIC PARTICLES FROM BECOMING WETTED UPON WORKING THEREBY CAUSING THE COMPOSITION TO LOSE ITS SENSITIVITY.
9. A composition according to claim 8 wherein the collector is a fatty acid.
10. A composition according to claim 9 wherein the fatty acid is oleic acid.
11. A composition according to claim 8 containing, in addition, a small amount of a frother to stabilize and control bubble size.
12. A composition according to claim 11 wherein the frother is selected from the group which consists of polypropylene glycol methyl ether and silicone resin.
Priority Applications (3)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
US444691A US3926698A (en) | 1974-02-21 | 1974-02-21 | Explosive compositions containing metallic fuel particles and method of preparation thereof |
CA220,469A CA1054799A (en) | 1974-02-21 | 1975-02-20 | Explosive compositions containing metallic fuel particles and method of preparation thereof |
JP50021393A JPS5811400B2 (en) | 1974-02-21 | 1975-02-20 | Bakuhatsu Sosebutsuto Sono Seihou |
Applications Claiming Priority (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
US444691A US3926698A (en) | 1974-02-21 | 1974-02-21 | Explosive compositions containing metallic fuel particles and method of preparation thereof |
Publications (1)
Publication Number | Publication Date |
---|---|
US3926698A true US3926698A (en) | 1975-12-16 |
Family
ID=23765950
Family Applications (1)
Application Number | Title | Priority Date | Filing Date |
---|---|---|---|
US444691A Expired - Lifetime US3926698A (en) | 1974-02-21 | 1974-02-21 | Explosive compositions containing metallic fuel particles and method of preparation thereof |
Country Status (3)
Country | Link |
---|---|
US (1) | US3926698A (en) |
JP (1) | JPS5811400B2 (en) |
CA (1) | CA1054799A (en) |
Cited By (9)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
FR2463110A1 (en) * | 1979-08-06 | 1981-02-20 | Du Pont | EXPLOSIVE EMULSION TYPE COMPOSITION AND PROCESS FOR PREPARING THE SAME |
FR2490213A1 (en) * | 1980-09-12 | 1982-03-19 | Ireco Chemicals | ANTIGRISOUTE EXPLOSIVE COMPOSITION CONTAINING CALCIUM NITRATE |
US5007973A (en) * | 1989-10-12 | 1991-04-16 | Atlas Powder Company | Multicomponent explosives |
USRE33788E (en) * | 1977-09-19 | 1992-01-07 | Hanex Products, Inc. | Water-in-oil blasting composition |
US5226986A (en) * | 1991-11-12 | 1993-07-13 | Hansen Gary L | Formulation of multi-component explosives |
US6361629B2 (en) * | 1998-11-12 | 2002-03-26 | The United States Of America As Represented By The Secretary Of The Air Force | Flowable solid propellant |
US20030084753A1 (en) * | 2001-11-05 | 2003-05-08 | Kim Chang Sun | Rapidly expanding metallic mixture treated to prevent oxidation thereof at room temperature |
US8585812B2 (en) * | 2011-05-26 | 2013-11-19 | Jackson State University | Oxygen displacement technology (ODT) to remove rust from iron and iron-based tools and structures |
US9573857B2 (en) | 2012-03-12 | 2017-02-21 | University Of Central Florida Research Foundation, Inc. | Compositions having aluminum particles dispersed in a continuous phase |
Citations (3)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
US3711345A (en) * | 1970-08-18 | 1973-01-16 | Du Pont | Chemical foaming of water-bearing explosives |
US3713919A (en) * | 1970-08-17 | 1973-01-30 | Du Pont | Chemical foaming of water-bearing explosives with n,n'-dimitrosopentamethylene-tetramine |
US3770522A (en) * | 1970-08-18 | 1973-11-06 | Du Pont | Emulsion type explosive composition containing ammonium stearate or alkali metal stearate |
-
1974
- 1974-02-21 US US444691A patent/US3926698A/en not_active Expired - Lifetime
-
1975
- 1975-02-20 JP JP50021393A patent/JPS5811400B2/en not_active Expired
- 1975-02-20 CA CA220,469A patent/CA1054799A/en not_active Expired
Patent Citations (3)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
US3713919A (en) * | 1970-08-17 | 1973-01-30 | Du Pont | Chemical foaming of water-bearing explosives with n,n'-dimitrosopentamethylene-tetramine |
US3711345A (en) * | 1970-08-18 | 1973-01-16 | Du Pont | Chemical foaming of water-bearing explosives |
US3770522A (en) * | 1970-08-18 | 1973-11-06 | Du Pont | Emulsion type explosive composition containing ammonium stearate or alkali metal stearate |
Cited By (11)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
USRE33788E (en) * | 1977-09-19 | 1992-01-07 | Hanex Products, Inc. | Water-in-oil blasting composition |
FR2463110A1 (en) * | 1979-08-06 | 1981-02-20 | Du Pont | EXPLOSIVE EMULSION TYPE COMPOSITION AND PROCESS FOR PREPARING THE SAME |
FR2490213A1 (en) * | 1980-09-12 | 1982-03-19 | Ireco Chemicals | ANTIGRISOUTE EXPLOSIVE COMPOSITION CONTAINING CALCIUM NITRATE |
US4364782A (en) * | 1980-09-12 | 1982-12-21 | Ireco Chemicals | Permissible slurry explosive |
US5007973A (en) * | 1989-10-12 | 1991-04-16 | Atlas Powder Company | Multicomponent explosives |
US5226986A (en) * | 1991-11-12 | 1993-07-13 | Hansen Gary L | Formulation of multi-component explosives |
US6361629B2 (en) * | 1998-11-12 | 2002-03-26 | The United States Of America As Represented By The Secretary Of The Air Force | Flowable solid propellant |
US20030084753A1 (en) * | 2001-11-05 | 2003-05-08 | Kim Chang Sun | Rapidly expanding metallic mixture treated to prevent oxidation thereof at room temperature |
US6849103B2 (en) * | 2001-11-05 | 2005-02-01 | Chang Sun Kim | Rapidly expanding metallic mixture treated to prevent oxidation thereof at room temperature |
US8585812B2 (en) * | 2011-05-26 | 2013-11-19 | Jackson State University | Oxygen displacement technology (ODT) to remove rust from iron and iron-based tools and structures |
US9573857B2 (en) | 2012-03-12 | 2017-02-21 | University Of Central Florida Research Foundation, Inc. | Compositions having aluminum particles dispersed in a continuous phase |
Also Published As
Publication number | Publication date |
---|---|
CA1054799A (en) | 1979-05-22 |
JPS5811400B2 (en) | 1983-03-02 |
JPS50117906A (en) | 1975-09-16 |
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Legal Events
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AS | Assignment |
Owner name: IRECO INCORPORATED A CORP OF DE Free format text: ASSIGNMENT OF ASSIGNORS INTEREST.;ASSIGNOR:IRECO CHEMICALS;REEL/FRAME:004350/0050 Effective date: 19840525 |