US3449180A - Explosive for blasting agent containing microcrystalline lipophilic ammonium nitrate - Google Patents
Explosive for blasting agent containing microcrystalline lipophilic ammonium nitrate Download PDFInfo
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- US3449180A US3449180A US676018A US3449180DA US3449180A US 3449180 A US3449180 A US 3449180A US 676018 A US676018 A US 676018A US 3449180D A US3449180D A US 3449180DA US 3449180 A US3449180 A US 3449180A
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- ammonium nitrate
- explosive
- lipophilic
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- 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 description 85
- 239000002360 explosive Substances 0.000 title description 47
- 238000005422 blasting Methods 0.000 title description 8
- 239000003795 chemical substances by application Substances 0.000 title description 8
- 239000000203 mixture Substances 0.000 description 47
- 150000003839 salts Chemical class 0.000 description 16
- XLYOFNOQVPJJNP-UHFFFAOYSA-N water Substances O XLYOFNOQVPJJNP-UHFFFAOYSA-N 0.000 description 15
- 238000005474 detonation Methods 0.000 description 12
- 239000000243 solution Substances 0.000 description 12
- 239000000295 fuel oil Substances 0.000 description 11
- 238000004880 explosion Methods 0.000 description 10
- -1 primary amino alkanes Chemical class 0.000 description 9
- 239000000126 substance Substances 0.000 description 9
- 229930195733 hydrocarbon Natural products 0.000 description 7
- 150000002430 hydrocarbons Chemical class 0.000 description 7
- 230000035945 sensitivity Effects 0.000 description 7
- 150000003973 alkyl amines Chemical class 0.000 description 6
- XAGFODPZIPBFFR-UHFFFAOYSA-N aluminium Chemical compound [Al] XAGFODPZIPBFFR-UHFFFAOYSA-N 0.000 description 6
- 238000009412 basement excavation Methods 0.000 description 6
- 239000000463 material Substances 0.000 description 6
- 125000002924 primary amino group Chemical class [H]N([H])* 0.000 description 6
- SNIOPGDIGTZGOP-UHFFFAOYSA-N Nitroglycerin Chemical compound [O-][N+](=O)OCC(O[N+]([O-])=O)CO[N+]([O-])=O SNIOPGDIGTZGOP-UHFFFAOYSA-N 0.000 description 5
- 229960003711 glyceryl trinitrate Drugs 0.000 description 5
- 229910002651 NO3 Inorganic materials 0.000 description 4
- NHNBFGGVMKEFGY-UHFFFAOYSA-N Nitrate Chemical compound [O-][N+]([O-])=O NHNBFGGVMKEFGY-UHFFFAOYSA-N 0.000 description 4
- 230000000052 comparative effect Effects 0.000 description 4
- 239000007788 liquid Substances 0.000 description 4
- 239000004576 sand Substances 0.000 description 4
- 238000003860 storage Methods 0.000 description 4
- QTBSBXVTEAMEQO-UHFFFAOYSA-N Acetic acid Chemical compound CC(O)=O QTBSBXVTEAMEQO-UHFFFAOYSA-N 0.000 description 3
- UEEJHVSXFDXPFK-UHFFFAOYSA-N N-dimethylaminoethanol Chemical compound CN(C)CCO UEEJHVSXFDXPFK-UHFFFAOYSA-N 0.000 description 3
- 229910000831 Steel Inorganic materials 0.000 description 3
- HCHKCACWOHOZIP-UHFFFAOYSA-N Zinc Chemical compound [Zn] HCHKCACWOHOZIP-UHFFFAOYSA-N 0.000 description 3
- 229910052782 aluminium Inorganic materials 0.000 description 3
- 230000005540 biological transmission Effects 0.000 description 3
- 229910052799 carbon Inorganic materials 0.000 description 3
- 238000001816 cooling Methods 0.000 description 3
- 229960002887 deanol Drugs 0.000 description 3
- 239000012972 dimethylethanolamine Substances 0.000 description 3
- HBRNMIYLJIXXEE-UHFFFAOYSA-N dodecylazanium;acetate Chemical compound CC(O)=O.CCCCCCCCCCCCN HBRNMIYLJIXXEE-UHFFFAOYSA-N 0.000 description 3
- 230000009977 dual effect Effects 0.000 description 3
- 238000001704 evaporation Methods 0.000 description 3
- 230000008020 evaporation Effects 0.000 description 3
- 238000002474 experimental method Methods 0.000 description 3
- 238000000034 method Methods 0.000 description 3
- 238000002156 mixing Methods 0.000 description 3
- 239000002002 slurry Substances 0.000 description 3
- 239000010959 steel Substances 0.000 description 3
- 229910052725 zinc Inorganic materials 0.000 description 3
- 239000011701 zinc Substances 0.000 description 3
- MXZROAOUCUVNHX-UHFFFAOYSA-N 2-Aminopropanol Chemical compound CCC(N)O MXZROAOUCUVNHX-UHFFFAOYSA-N 0.000 description 2
- LFQSCWFLJHTTHZ-UHFFFAOYSA-N Ethanol Chemical compound CCO LFQSCWFLJHTTHZ-UHFFFAOYSA-N 0.000 description 2
- 239000002253 acid Substances 0.000 description 2
- 238000013019 agitation Methods 0.000 description 2
- 150000001412 amines Chemical class 0.000 description 2
- ZCCIPPOKBCJFDN-UHFFFAOYSA-N calcium nitrate Chemical compound [Ca+2].[O-][N+]([O-])=O.[O-][N+]([O-])=O ZCCIPPOKBCJFDN-UHFFFAOYSA-N 0.000 description 2
- 239000013078 crystal Substances 0.000 description 2
- 238000002425 crystallisation Methods 0.000 description 2
- 238000004090 dissolution Methods 0.000 description 2
- 238000001035 drying Methods 0.000 description 2
- 229910052751 metal Inorganic materials 0.000 description 2
- 239000002184 metal Substances 0.000 description 2
- 239000004033 plastic Substances 0.000 description 2
- 239000000843 powder Substances 0.000 description 2
- 239000012047 saturated solution Substances 0.000 description 2
- VWDWKYIASSYTQR-UHFFFAOYSA-N sodium nitrate Chemical compound [Na+].[O-][N+]([O-])=O VWDWKYIASSYTQR-UHFFFAOYSA-N 0.000 description 2
- 238000001179 sorption measurement Methods 0.000 description 2
- ONDPHDOFVYQSGI-UHFFFAOYSA-N zinc nitrate Chemical compound [Zn+2].[O-][N+]([O-])=O.[O-][N+]([O-])=O ONDPHDOFVYQSGI-UHFFFAOYSA-N 0.000 description 2
- XIOUDVJTOYVRTB-UHFFFAOYSA-N 1-(1-adamantyl)-3-aminothiourea Chemical compound C1C(C2)CC3CC2CC1(NC(=S)NN)C3 XIOUDVJTOYVRTB-UHFFFAOYSA-N 0.000 description 1
- SPSSULHKWOKEEL-UHFFFAOYSA-N 2,4,6-trinitrotoluene Chemical compound CC1=C([N+]([O-])=O)C=C([N+]([O-])=O)C=C1[N+]([O-])=O SPSSULHKWOKEEL-UHFFFAOYSA-N 0.000 description 1
- GOLSFPMYASLXJC-UHFFFAOYSA-N 2-(dimethylamino)ethyl acetate Chemical compound CN(C)CCOC(C)=O GOLSFPMYASLXJC-UHFFFAOYSA-N 0.000 description 1
- HZAXFHJVJLSVMW-UHFFFAOYSA-N 2-Aminoethan-1-ol Chemical compound NCCO HZAXFHJVJLSVMW-UHFFFAOYSA-N 0.000 description 1
- UYKMMQPRRSJBAL-UHFFFAOYSA-N 2-hydroxypropanoic acid tetradecan-1-amine Chemical compound C(C(O)C)(=O)O.C(CCCCCCCCCCCCC)N UYKMMQPRRSJBAL-UHFFFAOYSA-N 0.000 description 1
- GDDNTTHUKVNJRA-UHFFFAOYSA-N 3-bromo-3,3-difluoroprop-1-ene Chemical compound FC(F)(Br)C=C GDDNTTHUKVNJRA-UHFFFAOYSA-N 0.000 description 1
- OKTJSMMVPCPJKN-UHFFFAOYSA-N Carbon Chemical group [C] OKTJSMMVPCPJKN-UHFFFAOYSA-N 0.000 description 1
- 239000004215 Carbon black (E152) Substances 0.000 description 1
- 244000007835 Cyamopsis tetragonoloba Species 0.000 description 1
- 239000001828 Gelatine Substances 0.000 description 1
- FYYHWMGAXLPEAU-UHFFFAOYSA-N Magnesium Chemical compound [Mg] FYYHWMGAXLPEAU-UHFFFAOYSA-N 0.000 description 1
- GRYLNZFGIOXLOG-UHFFFAOYSA-N Nitric acid Chemical compound O[N+]([O-])=O GRYLNZFGIOXLOG-UHFFFAOYSA-N 0.000 description 1
- 239000000020 Nitrocellulose Substances 0.000 description 1
- TZRXHJWUDPFEEY-UHFFFAOYSA-N Pentaerythritol Tetranitrate Chemical compound [O-][N+](=O)OCC(CO[N+]([O-])=O)(CO[N+]([O-])=O)CO[N+]([O-])=O TZRXHJWUDPFEEY-UHFFFAOYSA-N 0.000 description 1
- OAICVXFJPJFONN-UHFFFAOYSA-N Phosphorus Chemical compound [P] OAICVXFJPJFONN-UHFFFAOYSA-N 0.000 description 1
- 229920001131 Pulp (paper) Polymers 0.000 description 1
- QAOWNCQODCNURD-UHFFFAOYSA-N Sulfuric acid Chemical compound OS(O)(=O)=O QAOWNCQODCNURD-UHFFFAOYSA-N 0.000 description 1
- GSEJCLTVZPLZKY-UHFFFAOYSA-N Triethanolamine Chemical compound OCCN(CCO)CCO GSEJCLTVZPLZKY-UHFFFAOYSA-N 0.000 description 1
- 230000032683 aging Effects 0.000 description 1
- 125000000217 alkyl group Chemical group 0.000 description 1
- 229910045601 alloy Inorganic materials 0.000 description 1
- 239000000956 alloy Substances 0.000 description 1
- 239000002518 antifoaming agent Substances 0.000 description 1
- 239000010426 asphalt Substances 0.000 description 1
- 238000009835 boiling Methods 0.000 description 1
- 125000004432 carbon atom Chemical group C* 0.000 description 1
- 239000003245 coal Substances 0.000 description 1
- 239000011248 coating agent Substances 0.000 description 1
- 238000000576 coating method Methods 0.000 description 1
- 239000000084 colloidal system Substances 0.000 description 1
- 239000002283 diesel fuel Substances 0.000 description 1
- JRBPAEWTRLWTQC-UHFFFAOYSA-N dodecylamine Chemical compound CCCCCCCCCCCCN JRBPAEWTRLWTQC-UHFFFAOYSA-N 0.000 description 1
- 238000001914 filtration Methods 0.000 description 1
- 235000013312 flour Nutrition 0.000 description 1
- 239000012634 fragment Substances 0.000 description 1
- 229920000159 gelatin Polymers 0.000 description 1
- 235000019322 gelatine Nutrition 0.000 description 1
- 239000011521 glass Substances 0.000 description 1
- 238000005469 granulation Methods 0.000 description 1
- 230000003179 granulation Effects 0.000 description 1
- 238000010438 heat treatment Methods 0.000 description 1
- 238000011065 in-situ storage Methods 0.000 description 1
- 239000003999 initiator Substances 0.000 description 1
- 229910052500 inorganic mineral Inorganic materials 0.000 description 1
- 229910001959 inorganic nitrate Inorganic materials 0.000 description 1
- LIKBJVNGSGBSGK-UHFFFAOYSA-N iron(3+);oxygen(2-) Chemical compound [O-2].[O-2].[O-2].[Fe+3].[Fe+3] LIKBJVNGSGBSGK-UHFFFAOYSA-N 0.000 description 1
- 238000004519 manufacturing process Methods 0.000 description 1
- 235000012054 meals Nutrition 0.000 description 1
- 229910001092 metal group alloy Inorganic materials 0.000 description 1
- 150000002739 metals Chemical class 0.000 description 1
- 239000011707 mineral Substances 0.000 description 1
- 239000012452 mother liquor Substances 0.000 description 1
- 229910017604 nitric acid Inorganic materials 0.000 description 1
- 229920001220 nitrocellulos Polymers 0.000 description 1
- 229910052755 nonmetal Inorganic materials 0.000 description 1
- 150000002843 nonmetals Chemical class 0.000 description 1
- 239000007800 oxidant agent Substances 0.000 description 1
- 239000011574 phosphorus Substances 0.000 description 1
- 229910052698 phosphorus Inorganic materials 0.000 description 1
- 230000037452 priming Effects 0.000 description 1
- 239000003380 propellant Substances 0.000 description 1
- 239000011347 resin Substances 0.000 description 1
- 229920005989 resin Polymers 0.000 description 1
- 230000000717 retained effect Effects 0.000 description 1
- 239000011435 rock Substances 0.000 description 1
- 229920002545 silicone oil Polymers 0.000 description 1
- 239000004317 sodium nitrate Substances 0.000 description 1
- 235000010344 sodium nitrate Nutrition 0.000 description 1
- 239000001117 sulphuric acid Substances 0.000 description 1
- 235000011149 sulphuric acid Nutrition 0.000 description 1
- 239000000725 suspension Substances 0.000 description 1
- 239000011269 tar Substances 0.000 description 1
- UPCXAARSWVHVLY-UHFFFAOYSA-N tris(2-hydroxyethyl)azanium;acetate Chemical compound CC(O)=O.OCCN(CCO)CCO UPCXAARSWVHVLY-UHFFFAOYSA-N 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
- C01—INORGANIC CHEMISTRY
- C01C—AMMONIA; CYANOGEN; COMPOUNDS THEREOF
- C01C1/00—Ammonia; Compounds thereof
- C01C1/18—Nitrates of ammonium
Definitions
- ammonium nitrate as one component.
- These already known explosive mixtures consist, e.g., of 0 to 20% water, 3 to 6% hydrocarbons, and balance ammonium nitrate.
- These conventional explosive mixtures containing ammonium nitrate may additionally contain parafiin, asphalt, tar, wood pulp, sugar, meal, resins, coal, colloids that swell in water, metal powder, i.e., magnesium powder, aluminum powder, purely metallic alloys or alloys of metals and non-metals, i.e., phosphorus, used in a pulverulent or coarse state, or these materials may replace the above-mentioned hydrocarbons.
- Explosives or propellants containing inorganic nitrate, particularly ammonium nitrate, are also known which either contain nitrate as one component or are produced therefrom by treating said nitrate with 0.001 to 1.5 g. alkylamine, with at least 6 carbon atoms in the alkyl group per 100 g. of nitrate. This is to obtain a lower plastic viscosity and a lower yield point in the case of plastic explosives, and a greater density in the case of powdery explosives.
- the present invention relates to explosives or blasting agents containing ammonium nitrate which has been produced by crystallisation from concentrated or saturated solutions of ammonium nitrate in the presence of salts of primary amino alkanes in the amount of 0.1-5% by weight, preferably 0.2-1% by weight, their chain-lengths ranging from C C preferably from C C
- the object of the present invention is obtained in that the ammonium nitrate used consists entirely or in part of microcrystalline ammonium nitrate crystallised out in the presence of salts of amino alkanoles in the amount of 0.25% by Weight, preferably 0.4-1% by weight, and at a temperature between 20-90 C., having thus lipophilic characteristics.
- a lipophilic ammonium nitrate is produced from a mixture consisting of primary alkyl amines and primary to tertiary alkanolamines which is characterized by the fact that the surfaces of the ammonium nitrate crystals thus formed ice show the physical qualities of a carbon chain, whereby it is made possible that these surfaces hold liquid hydrocarbons or other organic liquids in a thermodynamically stable manner by means of adsorption.
- this adsorption aflinity towards hydrocarbons at room temperature cannot be maintained and preserved in a stable manner.
- ammonium nitrate according to the invention is the fact that the natural hydrophilic quality is not lost but even increased, apart from the added lipophilic quality, so that the ammonium nitrate produced according to the invention quite unexpectedly has the characteristic of being hydrophilic or lipophilic at the same time and according to desire.
- ammonium nitrate treated with alkyl amine has the tendency to increase its bulk density which is unfavourable or undesired in certain explosive mixtures.
- the ammonium nitrate produced according to the invention does not show such an increase in the bulk density.
- Alkyl amines and alkanolamines, or their organic or inorganic salts are added by agitation to the available or prepared ammonium nitrate solution, either separatel or in the form of a previously prepared mixture.
- a desired organic or mineral acid as, i.e., acetic acid or nitric acid
- an acid salt to the said solution, as, i.e., zinc nitrate, consequently adding a corresponding stoichiometrical amount of basic amine mixture in-situ for the purpose of producing a salt.
- crystallisation may be efiected by means of generally known devices or methods, e.g., crystallising out a solution by cooling with consequent filtration or centrifuging. A residual l-2% moisture is of no importance.
- the prepared mixtures may also evaporate in a vacuum at a steady temperature, thereby either obtaining a completely dry product, or interrupting the drying process as soon as the water contents has reached a certain percentage, or
- Lipophilic ammonium nitrate as such is an explosive relatively insensitive to ignition. Together with insignificant amounts of high explosives or simply by adding 3 to 6% of a hydrocarbon mixture highly brisant explosives or blasting agents are obtained showing characteristics that cannot be obtained with the same compositions made of conventional, crystalline, pulverulent ammonium nitrate.
- the entire oxidizing agent of the explosive composition does not necessarily have to consist of lipophilic ammonium nitrate; a part of it may be replaced by other salts, as, e.g., sodium nitrate or ammonium perchlorate.
- 10% by weight of lipophilic ammonium nitrate usually sufiice to improve the eifect and performance of the detonation.
- Examples 1 to 3 are a comparison between embodiments with amino alkanes on the one hand and amino alkanes and amino alkanoles on the other hand.
- Example 4 demonstrates the necessity to observe the temperatures
- Example 5 shows the advantageous characteristic which lies in the fact that the explosive or the blasting agent is not only of a lipophilic but also of a hydrophilic nature, which is quite astonishing when considering that these two qualities actually contradict each other.
- Examples 6 to 10 relate to a comparison between lipophilic ammonium nitrate and conventional ammonium nitrate.
- Example 11 describes the production of a slurry explosive by using a cooled solution without separating the mother liquir.
- EXAMPLE 1 (A) The following mixture is added to 10 kg. of a 80% ammonium nitrate solution with a temperature of 65 C.:
- the amine mixture is homogeneously mixed with the solution and subsequently permitted to cool to room temperature and to crystallise out during 24 hours without agitation.
- the crystals thus obtained are separated out by means of a Buchner funnel and pressed to a large extent. Analysis showed that the obtained ammonium nitrate still contains 3.2% moisture. Without further drying 200 g. fuel oil No. 4 are added to 4.800 g. lipophilic ammonium nitrate by means of a small laboratory mixer.
- mixture B was already insensitive towards detonators No. 6 and N0. 8 and the normal explosion characteristics could not be determined which serves as evidence for the fact that the unstable alkylamine coating (in the absence of alkanolamine) begins to decompose alter the cooling of the ammonium nitrate has come to an end.
- mixture A retained its sensitivity and its explosion characterist cs.
- EXAMPLE 2 (A) In a small laboratory vacuum evaporator (contents 20 liter) 12 kg. ammonium nitrate were heated in 2.1 1. water to a temperature of 85 C. Furthermore, g. tetradecylamine lactate and 120 g. 2-amino-2-methyl-1- propanol-lactate were added. Said vacuum evaporator was put into a water bath with a constant temperature of 85 C. Evaporation (at first boiling) was carried on for 3% hours, maintaining a vacuum of 80-30 torr. The product obtained contained 0.32% final moisture.
- ammonium nitrate B had turned almost completely into conventional ammonium nitrate after one week, said ammonium nitrate B being of the typical sandy and coarse nature and having furthermore a moist feel to it as if 1.25% water had been admixed to a conventional ammonium nitrate.
- ammonium nitrate A still proved to be pulverulent, dusty, and of a dry feel, in spite of its similar moisture contents, even after 6 months of storage.
- EXAMPLE 4 (A) The following solution was prepared in the laboratory vacuum evaporator of Example 2: 12 kg. ammonium nitrate plus 1.3 1. water, at a temperature of 102 C. 30 g. n-dodecyl-amine acetate and g. dimethyl ethanol amine acetate are added. The temperature of the water bath of the evaporator was adjusted at C.
- EXAMPLE 5 5 g. conventional ammonium nitrate and 5 g. ammonium nitrate produced according to the process of the present invention were weighed in two scales of 5 cm. diameter in layers as thin as possible, and then spread out. Both scales were then put into an air-tight glass container with a relative moisture of 75% (adjusted by means of a sulphuric acid solution of adequate vapor pressure). After remaining there for 24 hours analysis showed a 2.1% increase of weight in the case of the conventional ammonium nitrate. With the ammonium nitrate produced according to the method of the present invention the moisture pick up amounted to 7.5% increase of weight.
- the heating jacket of the evaporator was adjusted at 81- 83 C. After complete dissolution and mixing a vacuum of 6025 torr. was maintained during 3 hours. The ammonium nitrate obtained, which at the discharge had a temperature of 58 C., was packed into sacks, producing thus several tons of material in the same manner, stored and kept for further tests to be described below.
- the chosen aluminum quality was of a 99.5% purity and showed the following granulation:
- EXAMPLE 8 (A) Using the material of Example 6 as original substance 5 tons explosive in the following composition were produced:
- mixture B has the value 104, while mixture A reaches the unexpected value of 127.
- the differences are even more remarkable when comparing the brisance of these three types.
- the average volume of the rock fragments obtained by using mixture A is three times smaller than the one obtained when using mixtures B and C.
- the necessary secondary explosions after a large-scale detonation with mixture A amounted only to 20% of those necessary after a large-scale detonation with mixture B or C.
- EXAMPLE 9 Using 288 kg. of the lipophilic ammonium nitrate of Example 6 an explosive mixture was obtained by adding 12 kg. fuel oil No. 4. With a conventional cartridging device this mixture was packed into cartridges of 22 mm. diameter per mm. length.
- This example serves as evidence for the excellent ignition sensitivity of the explosive based on lipophilic ammonium nitrate without adding brisant explosives.
- An explosive agent comprising: ammonium nitrate, said ammonium nitrate comprising at least in part microcrystalline lipophilic ammonium nitrate, and
- said lipophilic ammonium nitrate having been produced by crystallizing a concentrated solution of ammonium nitrate in the presence of at least one salt of a primary amino alkane in the amount of from 0.1 to 5% by weight, having a chain-length between C and C and of at least one salt of an amino alkanol in the amount of from 0.2 to 5% by weight, at a temperature between 20 and C.
- said amount of said salt of a primary amino alkane is from 0.2 to 1% by weight.
- said chain-length of said salt of a primary amino alkane is from C12 to C14- 4.
- said amount of said salt of an amino alkano is from 0.4 to 1% by weight.
- the explosive agent of claim 1 containing between 3% and 6% hydrocarbons.
- the explosive agent of claim 5 containing between about 3% and 6% fuel oil and containing aluminum powder.
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Description
United States Patent US. Cl. 149-21 9 Claims ABSTRACT OF THE DISCLOSURE An explosive or blasting agent containing ammonium nitrate, the ammonium nitrate comprising at least in part microcrystalline lipophilic ammonium nitrate. The lipophilic ammonium nitrate is produced by crystallizing concentrated or saturated solutions of ammonium nitrate in the presence of salts of primary amino alkanes in the amount of from 0.1 to 5% by weight, having chainlengths ranging from C to C and in the presence of salts of amino alkanoles in the amount of from 0.2 to 5% by weight, at a temperature between 20 and 90 C.
Numerous explosives are already known which contain ammonium nitrate as one component. These already known explosive mixtures consist, e.g., of 0 to 20% water, 3 to 6% hydrocarbons, and balance ammonium nitrate. These conventional explosive mixtures containing ammonium nitrate may additionally contain parafiin, asphalt, tar, wood pulp, sugar, meal, resins, coal, colloids that swell in water, metal powder, i.e., magnesium powder, aluminum powder, purely metallic alloys or alloys of metals and non-metals, i.e., phosphorus, used in a pulverulent or coarse state, or these materials may replace the above-mentioned hydrocarbons.
Explosives or propellants containing inorganic nitrate, particularly ammonium nitrate, are also known which either contain nitrate as one component or are produced therefrom by treating said nitrate with 0.001 to 1.5 g. alkylamine, with at least 6 carbon atoms in the alkyl group per 100 g. of nitrate. This is to obtain a lower plastic viscosity and a lower yield point in the case of plastic explosives, and a greater density in the case of powdery explosives.
It is the aim of the present invention to improve explosives or blasting agents containing ammonium nitrate insofar as to considerably increase their brisance and ignition sensitivity. The present invention relates to explosives or blasting agents containing ammonium nitrate which has been produced by crystallisation from concentrated or saturated solutions of ammonium nitrate in the presence of salts of primary amino alkanes in the amount of 0.1-5% by weight, preferably 0.2-1% by weight, their chain-lengths ranging from C C preferably from C C The object of the present invention is obtained in that the ammonium nitrate used consists entirely or in part of microcrystalline ammonium nitrate crystallised out in the presence of salts of amino alkanoles in the amount of 0.25% by Weight, preferably 0.4-1% by weight, and at a temperature between 20-90 C., having thus lipophilic characteristics. In this manner a lipophilic ammonium nitrate is produced from a mixture consisting of primary alkyl amines and primary to tertiary alkanolamines which is characterized by the fact that the surfaces of the ammonium nitrate crystals thus formed ice show the physical qualities of a carbon chain, whereby it is made possible that these surfaces hold liquid hydrocarbons or other organic liquids in a thermodynamically stable manner by means of adsorption. When using only alkyl amines this adsorption aflinity towards hydrocarbons at room temperature cannot be maintained and preserved in a stable manner.
Another surprising characteristic of the ammonium nitrate according to the invention is the fact that the natural hydrophilic quality is not lost but even increased, apart from the added lipophilic quality, so that the ammonium nitrate produced according to the invention quite unexpectedly has the characteristic of being hydrophilic or lipophilic at the same time and according to desire.
Furthermore, it ought to be mentioned that ammonium nitrate treated with alkyl amine has the tendency to increase its bulk density which is unfavourable or undesired in certain explosive mixtures. However, the ammonium nitrate produced according to the invention does not show such an increase in the bulk density.
Alkyl amines and alkanolamines, or their organic or inorganic salts, are added by agitation to the available or prepared ammonium nitrate solution, either separatel or in the form of a previously prepared mixture. However, it is also possible to add at first a desired organic or mineral acid, as, i.e., acetic acid or nitric acid, to the ammonium nitrate solution, or to add an acid salt to the said solution, as, i.e., zinc nitrate, consequently adding a corresponding stoichiometrical amount of basic amine mixture in-situ for the purpose of producing a salt.
crystallisation may be efiected by means of generally known devices or methods, e.g., crystallising out a solution by cooling with consequent filtration or centrifuging. A residual l-2% moisture is of no importance. The prepared mixtures may also evaporate in a vacuum at a steady temperature, thereby either obtaining a completely dry product, or interrupting the drying process as soon as the water contents has reached a certain percentage, or
simply cooling the solution without separating the mother liquor, just as desired.
Lipophilic ammonium nitrate as such is an explosive relatively insensitive to ignition. Together with insignificant amounts of high explosives or simply by adding 3 to 6% of a hydrocarbon mixture highly brisant explosives or blasting agents are obtained showing characteristics that cannot be obtained with the same compositions made of conventional, crystalline, pulverulent ammonium nitrate. However, the entire oxidizing agent of the explosive composition does not necessarily have to consist of lipophilic ammonium nitrate; a part of it may be replaced by other salts, as, e.g., sodium nitrate or ammonium perchlorate.
In all explosives which contain ammonium nitrate the brisance and ignition sensitivity is increased if at least part of the ammonium nitrate consists of lipophilic ammonium nitrate. Thus, e.g., it was observed that an explosive mixture consisting of conventional ammonium nitrate, 0-3% water, and 3 to 6% hydrocarbons could not be ignited with a detonator No. 6. However, when using microcrystalline, lipophilic ammonium nitrate for an ammonium nitrate, then already those cartridges with a diameter of 20 mm. may be ignited with a detonator No. 6, ignition being efiected throughout a linear row of at least 30 cartridges with a diameter of 20 mm. and a length of mm.
10% by weight of lipophilic ammonium nitrate usually sufiice to improve the eifect and performance of the detonation.
The superiority of the explosives or blasting agents according to the present invention is demonstrated by the following examples. Examples 1 to 3 are a comparison between embodiments with amino alkanes on the one hand and amino alkanes and amino alkanoles on the other hand. Example 4 demonstrates the necessity to observe the temperatures, Example 5 shows the advantageous characteristic which lies in the fact that the explosive or the blasting agent is not only of a lipophilic but also of a hydrophilic nature, which is quite astonishing when considering that these two qualities actually contradict each other. Examples 6 to 10 relate to a comparison between lipophilic ammonium nitrate and conventional ammonium nitrate. Example 11 describes the production of a slurry explosive by using a cooled solution without separating the mother liquir.
EXAMPLE 1 (A) The following mixture is added to 10 kg. of a 80% ammonium nitrate solution with a temperature of 65 C.:
g. n-dodecylamine acetate, 75 g. triethanolamine acetate.
The amine mixture is homogeneously mixed with the solution and subsequently permitted to cool to room temperature and to crystallise out during 24 hours without agitation. The crystals thus obtained are separated out by means of a Buchner funnel and pressed to a large extent. Analysis showed that the obtained ammonium nitrate still contains 3.2% moisture. Without further drying 200 g. fuel oil No. 4 are added to 4.800 g. lipophilic ammonium nitrate by means of a small laboratory mixer.
(B) The same experiment was carried out at same conditions, however using only 25 g. n-dodecylamine acetate. Now the ultimate moisture amounted to 2.8%. Fuel oil No. 4 was also added to this mixture. By using explosive mixtures A and B the usual explosion characteristics of explosives were determined, which had been permitted to age for 1 day, 1 week, and 1 month.
l After one week mixture B was already insensitive towards detonators No. 6 and N0. 8 and the normal explosion characteristics could not be determined which serves as evidence for the fact that the unstable alkylamine coating (in the absence of alkanolamine) begins to decompose alter the cooling of the ammonium nitrate has come to an end. On the other hand mixture A retained its sensitivity and its explosion characterist cs.
EXAMPLE 2 (A) In a small laboratory vacuum evaporator (contents 20 liter) 12 kg. ammonium nitrate were heated in 2.1 1. water to a temperature of 85 C. Furthermore, g. tetradecylamine lactate and 120 g. 2-amino-2-methyl-1- propanol-lactate were added. Said vacuum evaporator was put into a water bath with a constant temperature of 85 C. Evaporation (at first boiling) was carried on for 3% hours, maintaining a vacuum of 80-30 torr. The product obtained contained 0.32% final moisture.
(B) At the same time a second equivalent chemical was prepared, however without the 2-amino-2-methyl-lpropanol-lactate. This ammonium nitrate contained a moisture of 0.22%. This time the ammonium nitrate of chemicals A and B was preserved without mixing and 4% fuel oil No. 4 was added after 1 week, 1 month, and 6 months.
After a 24-hour aging of these explosive mixtures the explosion characteristics were determined.
6 months 1 month 1 week B B B Excavation value according to Trauzl (net cmfi) Upsetting value according to Hess (dual strength steel disc),
Detonation speed according to Dautriche (zinc pipe. 30 mm. 5), m./sec
Detonation transmission (on sand) in 22 mm. e per 175 mm. length, cm
EXAMPLE 3 Two mixtures A and B were prepared according to Example 2, the only difference being that evaporation was interrupted after 3 hours. The final moisture of this ammonium nitrate was determined by analysis as follows:
In both cases explosive mixtures were produced with 4% diesel oil No. 4 after 1 week, 1 month, and 6 months of storage. Again chemical B was found to be insensitive to detonation. For chemical A the figures obtained were the same as in Examples 1 and 2.
The typical characteristic to be observed was that ammonium nitrate B had turned almost completely into conventional ammonium nitrate after one week, said ammonium nitrate B being of the typical sandy and coarse nature and having furthermore a moist feel to it as if 1.25% water had been admixed to a conventional ammonium nitrate.
On the other hand ammonium nitrate A still proved to be pulverulent, dusty, and of a dry feel, in spite of its similar moisture contents, even after 6 months of storage.
EXAMPLE 4 (A) The following solution was prepared in the laboratory vacuum evaporator of Example 2: 12 kg. ammonium nitrate plus 1.3 1. water, at a temperature of 102 C. 30 g. n-dodecyl-amine acetate and g. dimethyl ethanol amine acetate are added. The temperature of the water bath of the evaporator was adjusted at C.
(B) Another experiment was carried out in the following manner: 12 kg. ammonium nitrate are dissolved in 1.65 1. water at a temperature of 92 C., adding then the same amounts of n-dodecylic amine acetate and dimethyl ethanol amine acetate as in A. The temperature of the water bath of the evaporator was adjusted at 95 C.
(C) A third experiment was carried out, using 12 kg. ammonium nitrate in 2.1 1. water at a temperature of 82 C. and adding the same amounts of n-dodecylamineand dimethyl ethanol amine acetate as in A and B. The temperature of the water bath of the evaporator was kept constantly at 85 C. The period of evaporation was adjusted in such a way as to obtain an ammonium nitrate in the three instances A, B, and C, whose moisture contents ranged between 0.25 and 0.35%.
After a 1-day storage of these ammonium nitrate samples 2 kg. mixtures were produced in the following composition:
96% ammonium nitrate, 4% Fuel oil No. 4.
Excavation value according to Trauzl cm. 300 Upsetting value according to Hess (dual strength steel disc) mm 9.5 Detonation speed according to Dautriche (zinc pipe--30 mm. ..m./sec 3150 Detonation transmission on sand, in 22 mm. per 175 mm. length Zero negative For sample C high performance explosion data, as already known, were found out.
After having stored samples A, B, and C for one week these 2 kg.-mixtures were again prepared, consequentlyobserving an insensitivity towards detonators (No. 6 and No. 8) for chemicals A and B. Chemical C showed the same high performance explosion characteristics as before.
After another l-month and 6-month storage of sample C the corresponding explosive materials ofli'ered excellent explosive performances, very much like those of Example 2.
To round off this series of tests the ammonium nitrate chemicals A, B, and C were repeated again, this time however without adding dimethyl ethanolamine acetate. Just as in the case of the examples described above a rapid insensitivity towards detonators of the corresponding 4% fuel oil mixture was observed.
This series of tests also showed the necessity not to exceed an operating temperature of 90 C.
EXAMPLE 5 5 g. conventional ammonium nitrate and 5 g. ammonium nitrate produced according to the process of the present invention were weighed in two scales of 5 cm. diameter in layers as thin as possible, and then spread out. Both scales were then put into an air-tight glass container with a relative moisture of 75% (adjusted by means of a sulphuric acid solution of adequate vapor pressure). After remaining there for 24 hours analysis showed a 2.1% increase of weight in the case of the conventional ammonium nitrate. With the ammonium nitrate produced according to the method of the present invention the moisture pick up amounted to 7.5% increase of weight. This test was repeated in an atmosphere of 100% relative moisture, observing an increase of weight by 3.3% in the first instance (conventional ammonium nitrate) and a complete dissolution of the material in the second instance (lipophilic ammonium nitrate). These comparative tests serve to demonstrate the unexpectedly greater hidrophilic character of the lipophilic ammonium nitrate.
EXAMPLE 6 In an industrial vacuum evaporator with agitators of an available content of 1000 liter the following components were mixed and dissolved:
100 1. water,
600 kg. ammonium nitrate,
3.7 kg. zinc nitrate hexahydrate,
1.5 kg. n-dodecylamine,
6.0 kg. triethanolamine,
0.010 kg. silicone oil (anti-foam agent).
The heating jacket of the evaporator was adjusted at 81- 83 C. After complete dissolution and mixing a vacuum of 6025 torr. was maintained during 3 hours. The ammonium nitrate obtained, which at the discharge had a temperature of 58 C., was packed into sacks, producing thus several tons of material in the same manner, stored and kept for further tests to be described below.
6 The moisture of the lipophilic ammonium nitrate thus obtained ranged between 0.75 and 1.25%.
EXAMPLE 7 Using the lipophilic ammonium nitrate prepared in Example 6 as original substance the following explosive mixtures were prepared:
A B O D Lipophilic ammonium nitrate 96 93 84 73 Fuel oil N o. 4 4 4 4 3 Aluminum 0 6 12 24 For each of these explosive mixtures the following explosion characteristics could be observed:
In this connection it ought to be taken into considerae tion that pure blasting gelatine in the conventional composition 93/7 (93% nitroglycerine and 7% nitrocellulose) has an average excavation value of 560 cm.
The chosen aluminum quality was of a 99.5% purity and showed the following granulation:
Greater than 600 microns: 1%, Greater than 300 microns: 12%, Greater than 150 microns: 38%, Greater than 75 microns: 64%, Greater than 43 microns: 95%.
It is remarkable that extremely high weight strength (excavation value) is obtained neither when using coarser aluminum powder nor when using an extremely pulverulent, pyrotechnical powder. The excavation values for such mixtures containing a larger percentage of aluminum will generally not exceed 500 cm.
EXAMPLE 8 (A) Using the material of Example 6 as original substance 5 tons explosive in the following composition were produced:
96% lipophilic ammonium nitrate, 4% fuel oil No. 2.
(B) On the other hand 5 tons explosive were produced in the same composition, containing however conventional,
finely ground ammonium nitrate.
(C) Furthermore, 5 tons explosive were mixed in the same composition with a basis of porous prilled ammonium nitrate(prills).
On the basis of comparative explosions in an iron-ore mine with bore holes of 12 m. depth and 15 cm. diameter the following conclusion could be drawn:
Supposing the weight strength of mixture C to have a value of 100 according to definition, then mixture B has the value 104, while mixture A reaches the unexpected value of 127.
The differences are even more remarkable when comparing the brisance of these three types. The average volume of the rock fragments obtained by using mixture A is three times smaller than the one obtained when using mixtures B and C. The necessary secondary explosions after a large-scale detonation with mixture A amounted only to 20% of those necessary after a large-scale detonation with mixture B or C.
EXAMPLE 9 Using 288 kg. of the lipophilic ammonium nitrate of Example 6 an explosive mixture was obtained by adding 12 kg. fuel oil No. 4. With a conventional cartridging device this mixture was packed into cartridges of 22 mm. diameter per mm. length.
An approximately 20 m. long straight gutter was prepared on moistened sand. One after the other 100 of the cartridges mentioned above were put into this gutter. The priming cartridge which consists of the same mixture was initiated with a detonator No. 6. As a result the complete detonation of each of the 100 cartridges was observed.
This example serves as evidence for the excellent ignition sensitivity of the explosive based on lipophilic ammonium nitrate without adding brisant explosives.
However, it ought to be mentioned that, in contrast to conventional dynamites, these mixtures are not sensitive to impact. Comparative falling-weight tests with a drop hammer according to Kast showed that this mixture hardly detonates under the impact of a 5 kg. load which is dropped from a height of 1.5 m. Exactly the same result was obtained when using a pure ammonium nitrate sample. As is known, dynamites, even when pulverulent explosives with a low nitroglycerine content, will explode under the impact of a much smaller force.
EXAMPLE 10 Since direct comparative tests between explosive mixtures produced with lipophilic ammonium nitrate n the one hand and conventional ammonium nitrate on the other hand were not possible since the latter are insensitive towards detonators, the following tests were carried out:
94 parts by weight of finest ground ammonium nitrate was mixed with 4 parts by weight of fuel oil (No. 2 or No. 4), together with 2 parts by weight of liquid nitroglycerine. Although nitroglycerine had been added no sensitivity towards detonators could be observed.
With a second mixture of the same composition, containing however 4 parts by weight of nitroglycerine, only a marginal sensitivity towards detonator No. 8 could be observed. The explosion characteristics of such a mixture were the following:
Excavation value according to Trauzl (net cm. 280 Upsetting value according to Hess (dual strength steel disc) mm 4.7 Detonation speed according to Dautriche (zinc pipe-30 mm. m./sec 2450 Detonation transmission on sand, in 22 mm. per 175 mm. length cm Zero negative EXAMPLE 11 The following amounts of material were charged into a heatable agitating container:
kg. hot water (95 C.),
20 kg. of a 50% calcium nitrate solution (room temperature),
70 kg. ammonium nitrate.
At that point a white, comparatively liquid slurry was obtained. A suspension of 700 g. guar flour and 4.3 kg. fuel oil No. 2 was added, followed by another 5 minutes of mixing. A viscous slurry was obtained which showed an ignition sensitivity when using a 500 g. initiator booster (trinit-rotoluol, nitropenta, etc.) and which could be used for large-scale open pit detonations.
I claim: 1. An explosive agent comprising: ammonium nitrate, said ammonium nitrate comprising at least in part microcrystalline lipophilic ammonium nitrate, and
said lipophilic ammonium nitrate having been produced by crystallizing a concentrated solution of ammonium nitrate in the presence of at least one salt of a primary amino alkane in the amount of from 0.1 to 5% by weight, having a chain-length between C and C and of at least one salt of an amino alkanol in the amount of from 0.2 to 5% by weight, at a temperature between 20 and C.
2. The explosive agent, as set forth in claim 1, wherein:
said amount of said salt of a primary amino alkane is from 0.2 to 1% by weight.
3. The explosive agent, as set forth in claim 1, wherein:
said chain-length of said salt of a primary amino alkane is from C12 to C14- 4. The explosive agent, as set forth in claim 1, wherein:
said amount of said salt of an amino alkano is from 0.4 to 1% by weight.
5. The explosive agent of claim 1 containing between 3% and 6% hydrocarbons.
6. The explosive agent of claim 5 containing between about 3% and 6% fuel oil and containing aluminum powder.
7. The explosive agent of claim 1 wherein at least 10% by weight of the total ammonium nitrate content of said explosive agent is said lipophilic ammonium nitrate.
8. The explosive agent of claim 1, 2, 3, 4, 5, or 7, wherein said salt of an amino alkanol is an arnno ethanol or an amino propanol.
9. The explosive agent of claim 5 or 6 wherein at least 10% by weight of the total ammonium nitrate content of said explosive agent is said lipophilic ammonuim nitrate, and wherein said salt of an amino alkanol is a salt of an amino ethanol or an amino propanol.
References Cited UNITED STATES PATENTS 2,976,137 3/1961 Stengel l4946 X 2,978,864 4/1961 Stengel l4946 X 3,039,903 6/1962 Enokssom l4946 X 3,093,522 6/1963 Stengel et al l4946 3,166,452 l/l965 Gordon l4946 3,166,555 1/1965 Gordon l4946 X 3,303,073 2/1967 Graham l4946 X BENJAMIN R. PADGETT, Primary Examiner.
S. J. LECHERT, Assistant Examiner.
US. 01. X.R. 149 43, 44,46
UNITED STATES PATENT OFFICE CERTIFICATE OF CORRECTION Patent No. 3,449 ,180 June 10 1969 Marcel Vercauteren It is certified that error appears in the above identified patent and that said Letters Patent are hereby corrected as shown below:
In the heading to the printed specification, line 6, "Zundibutchen" should read Zundhutchen Signed and sealed this 5th day of May 1970.
(SEAL) Attest:
WILLIAM E. SCHUYLER, JR.
Edward M. Fletcher, Jr.
Commissioner of Patents Attesting Officer
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| AT1074666A AT277027B (en) | 1966-11-21 | 1966-11-21 | Process for the production of explosives or explosives |
Publications (1)
| Publication Number | Publication Date |
|---|---|
| US3449180A true US3449180A (en) | 1969-06-10 |
Family
ID=3624414
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| US676018A Expired - Lifetime US3449180A (en) | 1966-11-21 | 1967-10-18 | Explosive for blasting agent containing microcrystalline lipophilic ammonium nitrate |
Country Status (7)
| Country | Link |
|---|---|
| US (1) | US3449180A (en) |
| AT (1) | AT277027B (en) |
| BE (1) | BE703479A (en) |
| ES (1) | ES345628A1 (en) |
| GB (1) | GB1205245A (en) |
| LU (1) | LU54873A1 (en) |
| NO (1) | NO117412B (en) |
Citations (7)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| US2976137A (en) * | 1959-06-04 | 1961-03-21 | Commercial Solvents Corp | Ammonium nitrate explosives |
| US2978864A (en) * | 1958-05-19 | 1961-04-11 | Commercial Solvents Corp | Ammonium nitrate explosives |
| US3039903A (en) * | 1959-11-02 | 1962-06-19 | Nitroglycerin Ab | Explosive nitrate-alkylamine composition |
| US3093522A (en) * | 1959-01-14 | 1963-06-11 | Commercial Solvents Corp | Liquid fuels for reaction motors |
| US3166452A (en) * | 1962-06-06 | 1965-01-19 | Little Inc A | Explosive compositions containing ammonium nitrate-hexamethylenetetramine complexes |
| US3166555A (en) * | 1962-06-06 | 1965-01-19 | Little Inc A | Ammonium nitrate-hexamethylene-tetramine adduct |
| US3303073A (en) * | 1964-05-29 | 1967-02-07 | Canadian Ind | Ammonium nitrate-fuel oil explosive containing anti-static ingredinent |
-
1966
- 1966-11-21 AT AT1074666A patent/AT277027B/en not_active IP Right Cessation
-
1967
- 1967-09-05 BE BE703479D patent/BE703479A/xx unknown
- 1967-09-22 GB GB43357/67A patent/GB1205245A/en not_active Expired
- 1967-09-30 ES ES345628A patent/ES345628A1/en not_active Expired
- 1967-10-16 NO NO170145A patent/NO117412B/no unknown
- 1967-10-18 US US676018A patent/US3449180A/en not_active Expired - Lifetime
- 1967-11-15 LU LU54873D patent/LU54873A1/xx unknown
Patent Citations (7)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| US2978864A (en) * | 1958-05-19 | 1961-04-11 | Commercial Solvents Corp | Ammonium nitrate explosives |
| US3093522A (en) * | 1959-01-14 | 1963-06-11 | Commercial Solvents Corp | Liquid fuels for reaction motors |
| US2976137A (en) * | 1959-06-04 | 1961-03-21 | Commercial Solvents Corp | Ammonium nitrate explosives |
| US3039903A (en) * | 1959-11-02 | 1962-06-19 | Nitroglycerin Ab | Explosive nitrate-alkylamine composition |
| US3166452A (en) * | 1962-06-06 | 1965-01-19 | Little Inc A | Explosive compositions containing ammonium nitrate-hexamethylenetetramine complexes |
| US3166555A (en) * | 1962-06-06 | 1965-01-19 | Little Inc A | Ammonium nitrate-hexamethylene-tetramine adduct |
| US3303073A (en) * | 1964-05-29 | 1967-02-07 | Canadian Ind | Ammonium nitrate-fuel oil explosive containing anti-static ingredinent |
Also Published As
| Publication number | Publication date |
|---|---|
| GB1205245A (en) | 1970-09-16 |
| NO117412B (en) | 1969-08-04 |
| ES345628A1 (en) | 1969-05-16 |
| BE703479A (en) | 1968-02-01 |
| AT277027B (en) | 1969-12-10 |
| LU54873A1 (en) | 1968-02-05 |
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