US3711345A - Chemical foaming of water-bearing explosives - Google Patents
Chemical foaming of water-bearing explosives Download PDFInfo
- Publication number
- US3711345A US3711345A US00064793A US3711345DA US3711345A US 3711345 A US3711345 A US 3711345A US 00064793 A US00064793 A US 00064793A US 3711345D A US3711345D A US 3711345DA US 3711345 A US3711345 A US 3711345A
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- United States
- Prior art keywords
- water
- blasting
- fuel
- agent
- gas
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- Legal status (The legal status is an assumption and is not a legal conclusion. Google has not performed a legal analysis and makes no representation as to the accuracy of the status listed.)
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- 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
Definitions
- Water-bearing blasting agents are well known. These products typically comprise an oxidizing component, usually predominantly ammonium nitrate, a fuel component and water. More particularly, these blasting agents are referred to in the art as water-gels or slurry explosives, and emulsion type blasting agents.
- the blasting agents commonly referred to as water gels contain, in addition to the above ingredients, a thickening agent that gels the composition, e.g., guar gum or polyacrylamides.
- the water gels may contain high explosives such as TNT or metallic fuels such as aluminum that function not only as part of the fuel component of the blasting agent but also increase explosive strength.
- Emulsion type blasting agents contain at least one oxidizing agent, water, an emulsifying agent, and a fuel component that is a carbonaceous compound insoluble in water.
- the carbonaceous fuel used in the process for preparing these products is liquid during formation of the emulsion.
- the emulsifying agent generally forms a water-in-oil emulsion wherein oil is the continuous phase and water is the discontinuous phase of the emulsion.
- Representative water-bearing semisolid colloidal dispersions of emulsion type blasting agents are described in US. Pat. 3,447,978. Furthermore, these semisolid colloidal dispersions of water-bearing blasting agents, both the thickened water gel and emulsion type, have been prepared in such a manner that small gas bubbles are entrapped therein or they contain gas-entrapping material, e.g., microballoons. The inclusion of gas in the form of bubbles or in gas-entrapping material is known to regulate the strength of the blasting agent.
- Methods for preparing gas-containing water-bearing blasting agents include the mechanical incorporation of gas and in situ chemical generation of gas by the decomposition of certain compounds.
- This invention provides a process for preparing foamed semisolid colloidal dispersions of Water-bearing blasting agents, especially water gels 0r thickened water-bearing explosives, and emulsion type blasting agents, which comprises mixing inorganic oxidizing salt, fuel and water, the improvement which comprises incorporating into the mix an alkali metal borohydride gas-generating material thereby foaming and sensitizing the blasting agent.
- a thickening agent e.g., guar gum
- an emulsifying agent and a liquid carbonaceous fuel are added to the water-bearing explosive during preparation in order to form an emulsion between the water and fuel.
- the amount of alkali metal borohydride added to the mix is about from 0.002 to 0.10% based on the weight of the total composition.
- the gas-generating materials that are used in the proc ess of this invention are alkali metal borohydrides. These borohydrides decompose in the system and give oif gas at temperatures at which the blasting agent ingredients are formulated to produce a foamed product that is sensitized by small gas bubbles formed in the blasting agent. Any alkali metal borohydride can be used as the gasgenerating material in the present process. Representative alkali metal borohydrides that are used include lithium borohydride, potassium borohydride and sodium borohydride.
- gas-generating material used in the process varies and the specific amount employed depends upon the desired final density of the resulting product and the temperature of the formulation when the gas-generating agent is added thereto. Generally, amounts ranging from about 0.002 to 0.10% by weight, preferably 0.01 to 0.06%, are incorporated into the mix.
- the gas-generating agents are added to the composition at ordinary mixing temperatures, usually between to 170 F. However, for optimum results, the alkali metal borohydride gas-generating agent is added to the mix when the temperature of the mix is most favorable for decomposition of the foaming agent.
- the inorganic oxidizing salts used in this invention are those conventionally used in water-bearing blasting agents and include ammonium, alkali metal and alkaline earth metal nitrates and perchlorates as well as mixtures of two or more such salts.
- Representative inorganic oxidizing salts are ammonium nitrate, sodium nitrate, potassium nitrate, magnesium nitrate, calcium nitrate, ammonium perchlorate, sodium perchlorate, potassium perchlorate and magnesium perchlorate.
- the amount of inorganic oxidizing salt used in the water-bearing blasting agents is from about 20 to about 75% by weight of the composition.
- a mixture of inorganic nitrate salts is used of which at least about 45% by weight of the total composition is ammonium nitrate and of the order of 15 to 25%, preferably about 15%, based on the weight of the total composition, is sodium nitrate.
- the foamed semisolid colloidal dispersion of water-bearing blasting agents can contain a thickening agent to gel the composition, thus forming the well-known blasting agents known as water gels or slurry explosives.
- the amount of thickening agent added regulates the consistency of the blasting agent and such thickeners are used in amounts ranging from about 0.2 to Representative thickeners include galactomannans such as guar and locust bean gum; gum arabic; starches and modified starches such as dextrins, polyvinyl alcohol; polyacrylamides; high molecular weight polyethylene oxides; or mixtures of two or more of the above thickening agents. Best results are obtained when either guar gum or polyacrylamide is used as the thickener.
- this invention is applicable to the production of water and oil emulsion-type water-bearing blasting agents.
- These compositions contain, in addition to inorgamic oxidizing salt, water and fuel, and emulsifying agent.
- the amount of emulsifying agent used is from about 0.5 to by weight, and preferably from about 1 to 2%. Larger quantities of emulsifying agent may be added since excess emulsifying agent merely serves as a supplemental fuel for the blasting agent.
- the emulsifying agents used are those that form Water-in-oil emulsions, such as sorbitan fatty acid esters, e.g., soribtan monolaurate, palmitate or oleate; polyoxyethylene sorbitol esters and long chain fatty acids and esters thereof, so that a water-in-oil emulsion of the blasting agent is formed.
- the emulsifying agent is a stearate salt, e.g., sodium stearate, alone or in combination with stearic acid.
- emulsifying agents include sodium oleate with or without oleic acid, dodecylbenzene sulfonic acid and tall oil amides such as the tall oil amide of tetraethylene pentamide, EZ-Mul, manufactured by the Baroid Division of National Lead Co.
- the fuel-s used in thickened water gel blasting agents include self-explosive fuels, nonexplosive fuels and metallic fuels as well as mixtures of the aforementioned types of fuels.
- Representative self-explosive (fuels that can be used in the composition are organic nitrates, nitro compounds and nitra'mines such as trinitrotoluene, pentaerythritol tetranitrate, tetranitro-N-methylaniline, nitrostarch, explosive grade nitrocellulose, smokeless powder and mixtures thereof.
- the amount of self-explosive fuel used is from 10 to 40% by weight, based on the weight of the composition.
- Non-explosive fuels such as certain nitro aromatic hydrocarbons, for example, monoand dinitrobenzenes can be used, and sulfurous fuels including sulfur itself.
- Carbonaceous fuels such as finely-divided coal, hydrocarbons such as fuel oil and paraflin wax, can be added to the composition.
- Metallic fuels can also be used and these include light elements such as aluminum, magnesium, boron and silicon, both singly and in combination. Heavier metallic compounds and alloys including ferrophosphorus and ferrosilicon can be added to the mix.
- Blasting agents of the emulsion type wherein a water and oil emulsion is formed must contain carbonaceous fuel that is liquid during formation of the emulsion.
- the carbonaceous fuel is not soluble in water and generally forms the continuous phase of the emulsion so that the blasting agent is in the form of a water-in-oil emulsion.
- the carbonaceous fuel that is emulsified when used in the emulsion type blasting agents can include oil alone, a wax and oil, a wax and a polymeric material, or a wax and a polymeric modified oil component.
- the fuels used thus include hydrocarbons such as parafiinic, olefinic and aromatic that are saturted or unsaturated.
- Waxes that can be used include paraffin wax and mineral waxes. Petroleum oil of varying viscosities can be used as the fuel, especially fuel oil such as No. 2 [fuel oil.
- Polymeric materials such as natural or synthetic rubber may be used as a carbonaceous fuel component.
- the fuel comprises oil alone.
- the amount of fuel used is from about 3 to 10% by weight.
- the emulsion type blasting agents can contain supplementary fuels, as disclosed hereinabove, especially par- 7 4 a ticulate metals, e.g., aluminum, and finely-divided coal.
- the amount of fuel used in the blasting agents of the present invention is such that the oxygen balance of the blasting agent will be from 25 to +10% and preferably from 10 to +5
- the amount of water used in the blasting agents of the thickened water gel and emulsion type is from 5 to 30 percent by weight, preferably, about from 10 to 25 percent by weight water is used in preparing thickened water gels and emulsion-type blasting agents.
- nitrogen-base salts can be added to the water-bearing blasting agents to increase their effectiveness.
- the nitrogen-base salt functions, among other things, as a fuel component, and such salts that are applicable to this invention are disclosed, for example, in U.S. Pat. 3,431,155.
- the nitrogen-base salts used are monomethylammonium nitrate and ethylenediammonium dinitrate.
- Such salts can be added to the composition in amounts of from about 5 to 40% by weight.
- the composition can, and usually does, contain a crosslinking agent such as, for example, an alkali metal dichromate or a soluble antimony compound, e.g. potassium antimony tartrate, in amounts of from 0.001 to 1% by weight.
- a crystal habit modifier for the inorganic oxidizing salt such as Petro AG, which is a derivative of naphthalene sulfonic acid salts, can also be added to water gel compositions, if desired.
- the procedure for making thickened water gels is as follows. The oxidizer salts and other watersoluble materials are mixed with water at temperatures usually between about 140 and 170 F. to effect maximum solubility.
- the remaining ingredients except thickener, crosslinking agent and gas-generating material, are added.
- The-addition of these ingredients cools the mix.
- the mixture is agitated briefly and thickener added. Mixing is continued until thickening occurs, generally about 4 minutes; the alkali metal borohydride gas-generating material is added and the temperature of the mix is preferably about from to 150 F.
- the composition is mixed for about 30 seconds and then the crosslinking agent is added and a thickened [foamed blasting agent sensitized with gas bubbles is obtained.
- a procedure'for making emulsion type blasting agents involves mixing the emulsifiable carbonaceous fuel and emulsifier at a temperature of about to 170 F. such that the fuel is liquified. Separately, the inorganic oxidizing salts and other water-soluble materials are dissolved in water at about 120 to 170 F., and the other materials (except for the liquid fuel/ emulsifier mix) admixed therein. To this aqueous mixture is added the liquid fuel/emulsifier mix to form a water and oil emulsion.
- the temperature of the emulsion is usually about from 100 to F. or can be regulated therebetween, if desired; the emulsion begins to thicken and the gas-generating agent is added to the thickened emulsion.
- EXAMPLE 1 Formulation: Percent by weight Water 15.4 Ammonium nitrate 48.4265 Sodium nitrate 15.0
- the monomethylammonium nitrate fuel, 13/15 of the sodium nitrate and all of the ammonium nitrate were dissolved in water at 140 F.
- the thickener was premixed With sugar and the balance of the sodium nitrate was added to the ammonium nitrate solution together with the sulfur and coal.
- the mixture cooled to 100 F. as a result of the addition of the sodium nitrate as well as the result of heat loss by radiation, thickened, and sodium borohydride was added, followed by addition of the crosslinking agents.
- the specific gravity of the resulting foamed water gel blasting agent stabilized at 1.25 at ambient temperature and remained at that level for at least 30 days.
- EXAMPLE 2 EXAMPLE 3 Formulation: Percent by weight Ammonium nitrate 60.97 Water 17 Sodium nitrate 15 Fuel oil #2 EZ-Mul (tall oil amide of tetraethylene pentamine) 1 2 Ammonium nitrate, sodium nitrate and the tall oil amide of tetraethylene pentamine were mixed with the water at about 160 F. The fuel oil was added thereto when the mix was at 13O -140 F. and agitated to form a water-in-oil emulsion. The mixture started to thicken in about 2 minutes after agitation at which time the sodium borohydride was added to the thickened mix. Mixing was continued for about 1 minute to incorporate the foaming agent in the mix. The resulting water-in-oil emulsion blasting agent foamed and contained small gas bubbles of from about 20- to 100 microns in diameter. The blasting agent at 40 F. had a detonation velocity of about 5400 meters per second.
- EXAMPLE 4 The procedure described above in Example 3 was repeated except that potassium borohydride was substituted in place of sodium borohydride, and the emulsifying agent used was 2% sodium stearate. The resulting foamed emulsion blasting agent contained small gas bubbles. The blasting agent detonated at 40 F. with a detonation velocity comparable to that obtained in Example 3.
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Abstract
Description
Applications Claiming Priority (1)
Application Number | Priority Date | Filing Date | Title |
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US6479370A | 1970-08-18 | 1970-08-18 |
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US3711345A true US3711345A (en) | 1973-01-16 |
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US00064793A Expired - Lifetime US3711345A (en) | 1970-08-18 | 1970-08-18 | Chemical foaming of water-bearing explosives |
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Cited By (16)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
US3926698A (en) * | 1974-02-21 | 1975-12-16 | Ireco Chemicals | Explosive compositions containing metallic fuel particles and method of preparation thereof |
US4008108A (en) * | 1975-04-22 | 1977-02-15 | E. I. Du Pont De Nemours And Company | Formation of foamed emulsion-type blasting agents |
FR2323654A1 (en) * | 1975-09-11 | 1977-04-08 | Int Constr Prod Res | PROCEDURE AND COMPOSITION FOR CONTROLLING THE REMOVAL OF CEMENT MASS DURING SETTING, BY ADDITION OF AGENTS EMITTING GAS |
US4453989A (en) * | 1982-04-05 | 1984-06-12 | Atlas Powder Company | Solid sensitizers for water-in-oil emulsion explosives |
US4737207A (en) * | 1985-12-23 | 1988-04-12 | Nitro Nobel Ab | Method for the preparation of a water-in-oil type emulsion explosive and an oxidizer composition for use in the method |
US4933028A (en) * | 1989-06-30 | 1990-06-12 | Atlas Powder Company | High emulsifier content explosives |
US4980000A (en) * | 1990-01-17 | 1990-12-25 | Atlas Powder Company | Nitrostarch emulsion explosives production process |
US5051142A (en) * | 1990-01-17 | 1991-09-24 | Atlas Powder Company | Emulsion explosive containing nitrostarch |
US5089652A (en) * | 1990-01-17 | 1992-02-18 | Atlas Powder Company | Nitrate ester preparation |
FR2670203A1 (en) * | 1990-12-10 | 1992-06-12 | Dantex Explosives | AQUEOUS EXPLOSIVE COMPOSITION CONTAINING GAS BUBBLES STABILIZED WITH RESPECT TO MIGRATION AND AGGLOMERATION. |
US6537399B2 (en) | 1997-06-26 | 2003-03-25 | Union Espanola De Explosivos, S.A. | Process and mechanism for in situ sensitization of aqueous explosives |
US6610158B2 (en) | 1999-07-09 | 2003-08-26 | Union Espanola De Explosivos, S.A. | Procedure and installation for on-site manufacturing of explosives made from a water based oxidizing product |
US20040016481A1 (en) * | 2002-06-26 | 2004-01-29 | Union Espanola De Explosivos, A Spanish Corporation | Process for the "in situ" manufacturing of explosive mixtures |
US20090301619A1 (en) * | 2005-10-26 | 2009-12-10 | Newcastle Innovation Limited | Gassing of emulsion explosives with nitric oxide |
US20110132505A1 (en) * | 2007-01-10 | 2011-06-09 | Newcastle Innovation Limited | Method for gassing explosives especially at low temperatures |
EP3556741A1 (en) | 2018-04-16 | 2019-10-23 | Maxamcorp Holding, S.L. | Procedure and installation for loading boreholes with bulk water-based suspension or watergel type explosives |
-
1970
- 1970-08-18 US US00064793A patent/US3711345A/en not_active Expired - Lifetime
Cited By (20)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
US3926698A (en) * | 1974-02-21 | 1975-12-16 | Ireco Chemicals | Explosive compositions containing metallic fuel particles and method of preparation thereof |
US4008108A (en) * | 1975-04-22 | 1977-02-15 | E. I. Du Pont De Nemours And Company | Formation of foamed emulsion-type blasting agents |
FR2323654A1 (en) * | 1975-09-11 | 1977-04-08 | Int Constr Prod Res | PROCEDURE AND COMPOSITION FOR CONTROLLING THE REMOVAL OF CEMENT MASS DURING SETTING, BY ADDITION OF AGENTS EMITTING GAS |
US4453989A (en) * | 1982-04-05 | 1984-06-12 | Atlas Powder Company | Solid sensitizers for water-in-oil emulsion explosives |
US4737207A (en) * | 1985-12-23 | 1988-04-12 | Nitro Nobel Ab | Method for the preparation of a water-in-oil type emulsion explosive and an oxidizer composition for use in the method |
US4933028A (en) * | 1989-06-30 | 1990-06-12 | Atlas Powder Company | High emulsifier content explosives |
US4980000A (en) * | 1990-01-17 | 1990-12-25 | Atlas Powder Company | Nitrostarch emulsion explosives production process |
US5051142A (en) * | 1990-01-17 | 1991-09-24 | Atlas Powder Company | Emulsion explosive containing nitrostarch |
US5089652A (en) * | 1990-01-17 | 1992-02-18 | Atlas Powder Company | Nitrate ester preparation |
ES2051183A1 (en) * | 1990-12-10 | 1994-06-01 | Dantex Explosives | explosive composition |
FR2670203A1 (en) * | 1990-12-10 | 1992-06-12 | Dantex Explosives | AQUEOUS EXPLOSIVE COMPOSITION CONTAINING GAS BUBBLES STABILIZED WITH RESPECT TO MIGRATION AND AGGLOMERATION. |
US6537399B2 (en) | 1997-06-26 | 2003-03-25 | Union Espanola De Explosivos, S.A. | Process and mechanism for in situ sensitization of aqueous explosives |
US6610158B2 (en) | 1999-07-09 | 2003-08-26 | Union Espanola De Explosivos, S.A. | Procedure and installation for on-site manufacturing of explosives made from a water based oxidizing product |
US20040016481A1 (en) * | 2002-06-26 | 2004-01-29 | Union Espanola De Explosivos, A Spanish Corporation | Process for the "in situ" manufacturing of explosive mixtures |
US6949153B2 (en) | 2002-06-26 | 2005-09-27 | Union Espanola De Explosivos S.A. | Process for the “in situ” manufacturing of explosive mixtures |
US20090301619A1 (en) * | 2005-10-26 | 2009-12-10 | Newcastle Innovation Limited | Gassing of emulsion explosives with nitric oxide |
US8114231B2 (en) | 2005-10-26 | 2012-02-14 | Newcastle Innovation Limited | Gassing of emulsion explosives with nitric oxide |
US20110132505A1 (en) * | 2007-01-10 | 2011-06-09 | Newcastle Innovation Limited | Method for gassing explosives especially at low temperatures |
EP3556741A1 (en) | 2018-04-16 | 2019-10-23 | Maxamcorp Holding, S.L. | Procedure and installation for loading boreholes with bulk water-based suspension or watergel type explosives |
WO2019201851A1 (en) | 2018-04-16 | 2019-10-24 | Maxamcorp Holding, S.L. | Procedure and installation for loading boreholes with bulk water-based suspension or watergel type explosives |
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Legal Events
Date | Code | Title | Description |
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AS | Assignment |
Owner name: ETI EXPLOSIVES TECHNOLOGIES INTERNATIONAL INC., RO Free format text: ASSIGNMENT OF ASSIGNORS INTEREST.;ASSIGNOR:E.I. DU PONT DE NEMOURS AND COMPANY;REEL/FRAME:004834/0446 Effective date: 19880118 Owner name: ETI EXPLOSIVES TECHNOLOGIES INTE,STATELESS Free format text: ASSIGNMENT OF ASSIGNORS INTEREST;ASSIGNOR:E.I. DU PONT DE NEMOURS AND COMPANY;REEL/FRAME:004834/0446 Effective date: 19880118 |
|
AS | Assignment |
Owner name: TORONTO DOMINION BANK,STATELESS Free format text: SECURITY INTEREST;ASSIGNOR:ETI EXPLOSIVES TECHNOLOGIES INTERNATIONAL INC.;REEL/FRAME:004829/0868 Effective date: 19871231 Owner name: TORONTO DOMINION BANK Free format text: SECURITY INTEREST;ASSIGNOR:ETI EXPLOSIVES TECHNOLOGIES INTERNATIONAL INC.;REEL/FRAME:004829/0868 Effective date: 19871231 |