CA1244244A - Mix-delivery system for explosives - Google Patents
Mix-delivery system for explosivesInfo
- Publication number
- CA1244244A CA1244244A CA000453746A CA453746A CA1244244A CA 1244244 A CA1244244 A CA 1244244A CA 000453746 A CA000453746 A CA 000453746A CA 453746 A CA453746 A CA 453746A CA 1244244 A CA1244244 A CA 1244244A
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Abstract
ABSTRACT OF THE DISCLOSURE
Method and apparatus for making aqueous slurry explosives are disclosed. The components of the aqueous slurry explosive are mixed in a variable speed rotary mixer where the speed of the mixer is determined by the sequence of addition of the explosive components. The explosive components generally comprise water; an inorganic oxidizing salt such as ammonium nitrate;
organic liquid such as propylene glycol; organic solids such as sugar; air entraining agents such as microspheres; densifying agents such as hot ammonium nitrate solutions; thickening agents such as flours and guar gums and pH adjustors and self-explosives. The aqueous slurry explosive may be formed using ambient temperature water. The apparatus is particularly suited as a mobile unit for use in the field.
Method and apparatus for making aqueous slurry explosives are disclosed. The components of the aqueous slurry explosive are mixed in a variable speed rotary mixer where the speed of the mixer is determined by the sequence of addition of the explosive components. The explosive components generally comprise water; an inorganic oxidizing salt such as ammonium nitrate;
organic liquid such as propylene glycol; organic solids such as sugar; air entraining agents such as microspheres; densifying agents such as hot ammonium nitrate solutions; thickening agents such as flours and guar gums and pH adjustors and self-explosives. The aqueous slurry explosive may be formed using ambient temperature water. The apparatus is particularly suited as a mobile unit for use in the field.
Description
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FIELD OF T~IE INVENTION
__ _ This invention relates to aqueous slurry explosive mixtures ancl method and apparatus for their marluacture.
BACKGROUND OF THE INVENTION
Traditionally explosives have been prepared on site with metered flow provided by various auyers, vibrators and mixers feeding into pumps for delivery to blast holes in the material to be blasted. Uneven terrain, exposure to climate and lac]~ of quality control testing has normally resulted in poor blasting results.
Other methods using large concrete mixers require handling of extreme weights and are subject to differential segregation which provides poor repeatability in blasting. To improve on quality control, fixed plants using rigid quality control have been tried where the final product is shipped to the field in large containers and a pump is used to discharge the mixture for use. This system provides initially a better product but transportation over rough roads may result in segregation of the ingredients.
~0 Aqueous~slurry blasting compositions have been prepared in a variety of forms with a view to improving their reliability and stability in the field. United States patent 3,390,030 discloses an aqueous slurry blasting composition which employs the use o~ an aeration agent to lower the specific gravity of the composition and thereby improve its sensitivity. The aeration agent is in the form of a sodium nitrite or sodium bicarbonate which lowers the specific gravity of the aqueous slurry blasting agent at the time of blasting. The ammonium and sodium nitrates, as used in the blasting composition, are dissolved in a hot solution at approximately 140F, thus requiring the preparation of the composition in a plant operation.
The aqueous slurry also involves the use of ethylene glycol and guar gum as the thickener. The non-explosive carbonaceous fuel îs ground coal, although it is suggested that other carbonaceous fuels such as glycols, amine nitrates and granulated sugar may be used.
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, The use of aluminum as a sensitizer agent in ammoni~ml nitrate exp:Losives has become quite popular, as also exemplified in this patent. The flaked aluminum entraps air on its sur:Eaces assisting in inclusion oi:
tiny air bubbles in the slurr~. Such bubbles in an explosive serve to provide "hot spots" which help initiate the compositions.
Canadian patent 804,540 discloses an aerated aqueous slurry explosive composition using an inorganic oxidizing salt such as ammonium nitrate. Incorporating approximately 1% by weight of surfactant provides air entrainment within the composition. The air entrainment efficiency of the composition significantly improves the sensitivity of the composition to detonation by the high explosive pentaerythritol ketranitrate ~PETN~ boosters or the like. The slurry composition includes ammonium and sodium nitrate as the inorganic oxidizing agentO
Pine oil, ethylene glycol and guar gum are used as thickening agents in combination with sugar and flaked aluminum.
Many other forms of explosive compositions have been prepared and tried as exemplified in Canadian patent 610,246 which is directed to a basic ammonium nitrate explosive composition, where carbon is used as the sensitizer for the inorganic oxidizing agent.
Canadian patent 657,242 discloses the use of a heated solution in combin1ng the ammonium ni~rate into the explosive composition. Canadian patent 657,934 requires the use of a ~iinely divided ammonium nitrate with a~
liquifiable carbon such as fuel oil. Canadian p~tent 713,491 uses a surfactant in combination with nitric acid where the fuel material is essentially unreactive with the nitric acid component to provide a s~able composition. Canadian patent 829,23Q discloses the use of hexamethylene triamine~sensitizers for an ammonium nitrate explosive composition.
With the e~plosive compositions~disclosed in these patents, no attention has been directed to the mixing technique and as experience in the marketplace, these ~ ~.
:, :
composlti.ons are routinely mixed in various orms o~
rotatiny blade mixers ancl stirrers which are operated at a constant speed oE mix:i.ng.
The method, apparatus and aqueous slurry explosive mixture in accordance with this invention provides a composition which has improved performance, is economical to manufacture and the apparatus is particularly compact lending itself for use as a mobile unit.
SUMMARY OF THE INVENTION
.
According to an aspect of the invention, the apparatus mixes on a batch basis components of an aqueous sl.urry explosive mixture comprising:
i) 8~ to 25~ by weight water;
ii) 50% to 85~ by weight of an inorganic oxidizing salt selected from the group consisting of ammonium nitrate, alkali metal and alkaline earth metal nitrates and perchlorates, ammonium perchlorate and mixtures thereof;
iii) 2~ to 10% by weight of an organic liquid selected from the group consisting of ethylene glycol, propylene glycol, diethylene glycol, formamide, fuel oil, mineral oils and their emulsions and mixtures thereof, iv) 3~ to 15% by weight of an organic solid selected from the group consisting of sugar, hexamine, finely ground coal, sawdust, and pine needles and mixtuxes thereof, v) 0% to 6% by weight of air entraining agents selected from the group consisting of glass, Saran (trademark) or borate microspheresj perlite, ~ :
vermiculite, paint grade aluminum, milled aluminum, silicon, ferrosillcone, frothing aqents and mixtures thereof, : ~ :
vi) 0~ to 25~:by weight of densifying agents selected from the group consisting of barlte, magnetite, : hot ammonium nitrate solutions and mixtures `~ thereof, .
.
vii) 1% to 4% hy weight of thickening agents selected from the group consisting of flours, gumæ and mixtures thereof, viii) 0% to 25% by weight of ancillary components selected from the group consisting of catalysts, pH
adjusters and a self-explosive.
The improvement in the apparatus comprises a variable speed rotary mixer in which explosive components, as added to the mixer, are mixed at various rotational speeds which are predetermined by the sequence of addition of components.
The use of this type of mixer in formulating batches of explosive compositions lends itself to use on a mobile unit. This arrangement, therafore, avoids preparation of the compositions at the plant and ready use in the field to avoid the problems with transportation of the prepared materials from the plant to the field. Accordingly, the invention provides a mobile mixing plant for mixing on a batch basis components of an aqueous slurry explosive mixture. The mobile plant comprises a plurality of storage tanks for individual components to be mixed. A rotary mixer mixes the components. Each storage tan~ has means for transferring a batch quantity of the respective explosive slurry component to the mixer. A variable speed drive rotates the mixer. Means is provided for controlling the variable speed drive to rotate the mixer at various rotational speeds which are predetermined by~
~ 30 ths sequence of addition of the components to the mixer.
~11 of the individual components introduced to the mixer remain in the mixer until completely mixed by the rotary mixer into an aqueous slurry explosive mixture. Means is provided for withdrawing the aqueous slurry explosive mixture from the mixer.
According to another aspect of the invention, the method for preparing the explosive composition comprises mixing at a first speed in the mixer 10 to 20 parts by weight of ambient temperature water with 3 to 12 parts by weight of sugar and 9 to 5 parts by weight of an air ;
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bubble entraining agent other than paint fine aluminum.
Mixing is continued at this ~irst speed and 50 to 85 parts by weight of ground ammonium nitrate is added.
After addition the mixing speed is increased to a second speed in forming a saturated solution o~ ammonium nitrate. At this second speed, 0 to 5 parts by weight of paint fine aluminum in a plastic mesh binding is - mixed. A dispersion of 1 to 4 parts by weight of guar gums and 2 to 6 parts by weight of ethylene glycol is added and mixing continued at the second speed. The mixing speed is reduced to the first speed when complete distribution of the components is achieved and mixing is continued at the first speed until the guar gum content is completely hydrated.
BRIEF DESCRIPTION OF DRAWINGS
Preferred embodiments of tha invention are shown in the drawings wherein:
Figure 1 is a schematic of the apparatus according to this invention adapted for use as a mobile unit.
DETAILED DESCRIPTION OF TH~ PREFERRED EMBODIMENTS
The apparatus, according to this invention, is adapted for use in mixing small batches of up to 5,000 pounds of aqueous slurry explosive mixtures. The batches are of a size such that, when mixed by the apparatus of this invention, a homogeneous consistent explosive mixture with reliable performance is produced.
The apparatus 10, as shown in Figure 1, is adapted for use on a mobile unit 12 having truck cab 14 and flat bed 16. The apparatus 10 is secured to the flat bed 16 where the rotary mixer 18 is supported on the flat bed 16 by posts 20 and 22~ The mixer 18, according to this preferred embodiment, is a double ribbon rotary mixer having a tank 24 which is semi-circular in cross-section along its bottom 26. According to an embodiment of the invention, the tank 24 may be cylindri¢al where the end walls 28 and 30 are upright and planar. The shaft 32 for the mixer is bearingly mounted in the walls by bearings 34 where the shaft extends outwardly~of end wall 28 to be driven by motor 36. Secured to the shaft is an outer helical ribbon bar 38 which is connected to , `:
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the shaft by radial arms 40. I'he outer helical ribbon bar extends along ancl is symmetrical about the shaft.
Similarly, an inner ribbon bar 42 is secured to the shaft by shorter arms 44 and extends along ancl is symmetrical about the shaft. The outer helical ribbon bar 38 extends alony the tank in a first rotational direction and the inner helical ribbon bar 42 extends along the tank in a second rotational direction opposite to that of the first rotational direction. This arrangement for the double ribbon mixer bars induces a forward and a reverse flow to the mixture in providing continuous shear blending oE the mixture components.
According to a preferred embodiment of this invention, there are two sets of the inner and outer helical ribbon bars in the double ribbon mixer blender 18. It is appreciated that other types of mixers may be used with the variable speed feature of this invention for mixer explosives. Other types of mixers include blade type and paddle type.
Preferably the bottom portion 26 of the mixer tank 24 is sloped towards the outlet 46 which has a control valve 48 for passage of the mix components via conduit 50 to pump 52. It is appreciated that other forms of rotary mixers may be used,~such as rotary paddle mixers, blade mixers and the like. The important aspect of these mixers is that they have variable speed facility.
The components for the aqueous slurry explosive mixture are stored in storage tanks 54, 56, 58, 60 and 62. The mixed product, when taken off the mixing tank 24, is pumped by pump 52 into the slurry explosive ;
mixture storage tank 64. It is appreciated that the storage tank 64 is optional in that the mixture when taken off the mixing tank 24 may be pumped directly via ~ hose~66 into the bore holes.~ ~
- ~ Storage tank 54 stores the ammomium nitrate 68 whi~h is ground by a stainless steel hammer mill 70.
The ground material falls onto the base 72 of auger 74 which is driven by hydraulic motor 76. The ground ammomium nitrate is augered up to inlet 78 for ., - ' ~2~
introduction to within the mixing tank 724. The microspheres 80 are stored in tank 56 and a quantity thereof is introduced to the mixiny tank 24 via conduit 82 as controlled by valve 84. Storage tank 58 is for the thickening agents which may be guar gum and ethylene glycol. These components are mixed by stirrer 86 which is driven by hydraulic motor 88. ~he mixed thickening agents are introduced to the mixing tank via conduit 90 as controlled by valve 92~
Storage tank 60 may be used as the water metering tank containing ambient temperature water 94. A site glass may be provided on the side of the tank to indicate the quantity of water being dispensed via conduit 96 into the mixing tank as controlled by control valve 98~ The storage tank 62 may be used to store the batch weight of sugar 100 which is dispensed via conduit 102 into the mixing tank as controlled by control valve 104.
In addition to hydraulic motors 36, 76, 88, hydraulic motors ara also provided for driving pump 52 and a pump (not shown) in the hose reel 67. For each hydraulic motor is a set of lines such as 106 and 108 for hydraulic motor 76. A cont:rol device 110 is provided for controlling the flow of pressurized hydraulic fluid in the linas 106, 108 to the various motors. The pressurized hydraulic fluid may be provided to the controller 110 by way of a hydraulic pump mounted on a power take of~ from the engine compartment 112 of the mobile unit. By way of a manifold arrangement, the pressurized fluid may be distributed tG the various lines 106, 108 for each of the hydraulic motors as determined by the controller 110. Switches 114 and 116 are provided for the motors on pump 52 and the pump within the hose reel 67. Since these pumps are not of variable speed, simple on/off switches are all that is required. For hydraulic motor 36, rotary valve 118 is provided to control the ~low rate of the hydraulic fluid in the lines ~06, 108 to motor 36, where by calibration the speed at which the shaft 32 is turning is read out ~3 on meter 120. Similarly, control valve 122 in combination with meter 124 determines and indicates the speed of the motor 88 for the stirrer 86. The hydraulic motor 76 is controlled by variable control valve 126 where its speed is indicated on meter 128.
In accordance with the sequence of additions of the various components for the explosive mixture, the speed at which the rotary mixer 18 is driven is determined by the control valve 118, the details of which will be explained with respect to Examples demonstrating the mixing of preferred compositions. The controller 110 is set up to provide a ranye of mixing speeds in the rotary mixer varying from approximately 20 rpm to approximate.ly 100 rpm.
It is appreciated that in the pumping arrangement to economize on the number of pumps used in handling the slurried explosive, the conduit and valving arrangement may be modified so that pump 52 may be used to not only transfer the mixed slur~y composition into storage tank 64, but also be used to withdraw the explosive mixture from the tank 64 via outlet conduit 130 and pump it ~; through the hose 66 thereby eliminating the pump and the hose reel 67. This may be accomplished by rerouting conduit 130 to the inlet 50 of pump 52 and providing a T-section on the outlet of pump 52 where, in addition to conduit 132 which transfers the mixed slurry to the storage tank 64, there is a second conduit which is interconnected to the hose reel 67.
The apparatus, according to this invention, is useful in preparing many forms of aqueous slurry explosive mixtures. In general, the apparatus according to this invention may be used to mix explosive mixtures which have the following composition:
i) 8~ to 25% by weight water;
ii) 50% to 85~ by weight of an inorganic oxidizing salt selected from the group consisting of ammonium nitrate, alkali metal and alkaline earth metal nitrates and perchlorates, ammonium perchlorate and mixtures thereof;
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iii) 2~ to 10% by weight of an organic liquid selected ~rom the grollp consisting of ethylene ylycol, propylene glycol, cliethylene ylycol, formamide, Euel oil, mineral oils and their emulsions and mixtures thereof, iv) 3% to 15% by weight of an oryanic solid selected from the group consisting of sugar, hexamine, finely ground coal, sawdust, and pine needles and mixtures thereof, v) 0% to 6% by weight of air entraining agents selected from the group consisting of glass, Saran (trademark) or borate microspheres, perlite, vermiculite, paint grade aluminum, milled aluminum, silicon, ferrosilicone, frothing agents and mixtures thereof, vi) 0% to 25% by weight of densifying agents selected from the group consisting of barite, magnetite, hot ammonium nitrate solutions and mixtures thereof, vii~ 1~ to 4% by weight of thickening agents selected from the group consisting of flours, gums and mixtures thereof, viii) 0~ to 25% by weight of ancillary components selected from the group consisting of catalysts, pH adjusters and a self-explosi~e.~
Th.is product may be either packaged for later loading or pumped in bulk form down blast holes.
Conventional priming devices, such as blasting caps,; ~ ;
cast primers or detonating cord, may be used to initiate these products with exceptional and reproducable :
results. The priming devices may be of the well known variety used, such as PETN (pentaerythritol tetranitrate), TNT, RDX (cyclotrimethylenetrinitra amine), Tetryl or the like. ~ ; ~
The inorganic oxidiæing component includes nitrate fertilizers in prill form, particulated form and in solution. These nitrate fertilizer mixtures may include ammonium nitrate, sodium nitrate, calcium nitrate, and other metal nitrates. Also perchlorates or , :. : :
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pe~manganates of ammonia. The blending of the ammonium nitrates and the like in the slurry composition i~
conducted with cold wa-ter, that is water at a~bient temperature. There is no neecl to heat the wa~er used in the system in forming the saturated solution ~or the ammonium nitrate mixture. Normally the water is at 40F
and thereby forming a saturated solution at this temperature, where normally the temperature does not exceed this level. In so doing, we do not ~orm crystals in the slurry as compared to systems which may use hot water in dissolving the ammonium nitrate which upon cooling can form growth masses of insensitive ammonium nitrate crystals, thereby affecting the reproducibility of the blasting power of the composition Various fuels are used which may include glycol f sugar, carbon commuted to -30 mesh, fuel oil, hexamines and formamide. It is understood that the term sugar covers any form of suitable sugar substance, such as standard granular sucrose, dextrose and the like which can be used in an explosive mixture as a carbon source.
Explosives may be used such as TNT, PETN, or fine grained smokeless powders. Metals such as aluminum, silicon, ferrosilicon; metal oxides such as barite or magnetite may be included as fuels or densifying agents.
Emulsifiers may be required to suspend certain liquid fuels.
Since heat transfers within the explosive is assisted by adiabetic compression of the micro air bubbles, inclusion and distribution of these ~ubbles lS
preferable to ensure detonation with no self-explosive in the slurry composition. Suitable agents for incorporating micro air bubbles are frothers, such~as Deriphat (trademark), micro balloons, such as made from Saran ~trademark), glass or borates and low density metals which have been rolled to entrap air while being ground, such as certain aluminum powders commonly known ~ as paint fine aluminum.
; To provide long term storage in either package form or down the bore hole bulk form, guar gum is , ll l Z~J~
selected optionally containing suitable catalysts. The mixture iB kept at suitable pH with appropriate bufEering agents, such as ammonium hydroxide or nitric acid until the final point of use. A parid pH change may be induced by ammonium gas solution, nitric acid mixtures or sodium dichromate solution. This creates a final product known as a gel which is water reslstant and thus very useful in bore hole applications.
~he apparatus 10, as used in mixing the slurry, may have premeasured amounts of each of the components for the mixture, so that the exact amount in each of the storage tanks 54, 56, 58 60, and 62 are introduced to the mixing tank 24. In the alternative, where smaller batches of explosive are required, various types of metering and weighing devices (not shown) may be used so that the axact proportions of the mixture components can be introduced to the mixing tank 24 for mixing. It is appreciated, of course, that the mixing tank 24 will have upper and lower limits in terms of the amount for each batch to be mixed. Preferably in mobile units, the mixing tank 24 is of a size that will handle ranges in batch compositions of 500 to 5000 lbs.
An aqueous slurry explosive of the following composition range is made up as follows:
i~ 10% to 20% by weight of water, ii) 3% to 13% by weight of sugar, iii) 1% to 5~ by weight of an air entraining agent selected from the group consisting of borate microspheres, glass microspheres, Saran microspheres and milled aluminum of 5 to 20 ~ particle size, iv) 50% to 85% by weight of ammonium nitrate, v~ 2% to 6% by weight of ethylene glycol, vi) 1% to 4% by weight of guar gums, vii) 0% to 15% by weight of ground aluminum as a th~rmal energy additive.
Based on 100 parts by weight, the following specific composition was mixed: 13 part~ by weight of water was introduced to the mixer, then 10 parts by weight of . ~.
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sugar and 2 parts by weighk of Q-cells ( trademark) (microspheres oE tiny hollow part.icles that encapsulate air in a spherical shell) we,re added to the mixer and blended completely for approximately 2 minutes at a speed of 40 rpm. Seventy-two parts by weight of crushed ammonium nitrate was added while blending at 40 rpm.
When all ammonium nitrate was added, the mixer speed was increased to 80 rpm for 2 minutes.
One part by weight and 2 parts by weight of guar gums and glycol were mixed in the stirrer storage tank 58 and introduced to the mixer which continued mixing at 80 rpm. When complete distribution was achieved, the mixer speed was lowered to 40 rpm until the guar gums were completely hydrated. The composition was then ready for transfer to the bore holes or storage in the storage tank 64.
It has been found that the explosive composition is particularly inexpensive to manufacture and has a good explosive property. The following table compares the power of the above specific composition to known materials, POWER OF SUGAL GEL
Weight Energy Bulk Energy~ Density Product Kilocalories/Gram Kilocalories/cc GMS/cc _ _ ~ . ~ _ ANFO 0.84 0.69 0.83 (Ammonium Nitrate Y
Fuel oil 30 Explosive ~ ~ ~
Standard 0.7972 ~ 1.1161 1.40 TNT Slurry ~ ~ ~
Specific 0.6298 0.7872 1~25 Mix of this Invention ~ ........ ,.. 0.. _~.. _ I
Production blasting confirmed that the product without aluminum additives compares favourably to ANFO
on a bulk energy basis. As with all water gels, :
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aluminum Euels may be used to add linearly to the power.
Fuel grade aluminum may be used in these compositions to provide higher strengths. Up to a level of approximately 15~ by weight oE aluminum may be used.
The fuel yrade aluminum is usually through -30 mesh and retained on a ~100 mesh screen. The paint fine aluminum in a ~eflon mesh is added to the mixture at the higher mixer speed of 80 rpm. This higher speed properly dispenses the aluminum fines throughout the mixture.
The variable speed rotary mixer is particularly useful in blending the microspheres without breakage.
Equal utility is ~ound in dispensing paint fine aluminum which has the "Teflon" (trade mark of Dupont for a fluorocarbon resin) mesh bonding the aluminum fines.
This does not disperse properly during normal mixing.
However in using the double ribbon blender at variable speeds, the desired mixing is achieved in forming a uniform dispersion of the aluminum fines through the mix without wetting the aluminum and thereby driving off the micro air bubbles trapped on the aluminum fines during milling. Because of the efficiency of the mixer, a compact arrangement is provided for ~he apparatus which lends itself readily for use on mobile units. Thus the unit may be driven to the field with the components unmixed, thereby avoiding segregation of premixed components. The system~may then prepare the desired amount of explosive composition for dispersal through the hose 66 to the various bore holes in the material to be blasted. Also because of its compactness, the apparatus may be used in underground mines to ensure balancing of the oxidizing components so that poisonous gases ater an explosion are Xept to a minim~m. This~is accomplished by ensuring an oxygen balance in the composition as prepared with the components uni~ormly dispersed throughout the mixture by the mixer.
Although preferred embodiments of the invention have been described herein in detail, it will be understood by those skilled in the art that variations ~,~
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may be made thereto wlthout departing frorn the spirit of the invention or the scope o~ the appended claims.
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FIELD OF T~IE INVENTION
__ _ This invention relates to aqueous slurry explosive mixtures ancl method and apparatus for their marluacture.
BACKGROUND OF THE INVENTION
Traditionally explosives have been prepared on site with metered flow provided by various auyers, vibrators and mixers feeding into pumps for delivery to blast holes in the material to be blasted. Uneven terrain, exposure to climate and lac]~ of quality control testing has normally resulted in poor blasting results.
Other methods using large concrete mixers require handling of extreme weights and are subject to differential segregation which provides poor repeatability in blasting. To improve on quality control, fixed plants using rigid quality control have been tried where the final product is shipped to the field in large containers and a pump is used to discharge the mixture for use. This system provides initially a better product but transportation over rough roads may result in segregation of the ingredients.
~0 Aqueous~slurry blasting compositions have been prepared in a variety of forms with a view to improving their reliability and stability in the field. United States patent 3,390,030 discloses an aqueous slurry blasting composition which employs the use o~ an aeration agent to lower the specific gravity of the composition and thereby improve its sensitivity. The aeration agent is in the form of a sodium nitrite or sodium bicarbonate which lowers the specific gravity of the aqueous slurry blasting agent at the time of blasting. The ammonium and sodium nitrates, as used in the blasting composition, are dissolved in a hot solution at approximately 140F, thus requiring the preparation of the composition in a plant operation.
The aqueous slurry also involves the use of ethylene glycol and guar gum as the thickener. The non-explosive carbonaceous fuel îs ground coal, although it is suggested that other carbonaceous fuels such as glycols, amine nitrates and granulated sugar may be used.
~a~
.
':
, The use of aluminum as a sensitizer agent in ammoni~ml nitrate exp:Losives has become quite popular, as also exemplified in this patent. The flaked aluminum entraps air on its sur:Eaces assisting in inclusion oi:
tiny air bubbles in the slurr~. Such bubbles in an explosive serve to provide "hot spots" which help initiate the compositions.
Canadian patent 804,540 discloses an aerated aqueous slurry explosive composition using an inorganic oxidizing salt such as ammonium nitrate. Incorporating approximately 1% by weight of surfactant provides air entrainment within the composition. The air entrainment efficiency of the composition significantly improves the sensitivity of the composition to detonation by the high explosive pentaerythritol ketranitrate ~PETN~ boosters or the like. The slurry composition includes ammonium and sodium nitrate as the inorganic oxidizing agentO
Pine oil, ethylene glycol and guar gum are used as thickening agents in combination with sugar and flaked aluminum.
Many other forms of explosive compositions have been prepared and tried as exemplified in Canadian patent 610,246 which is directed to a basic ammonium nitrate explosive composition, where carbon is used as the sensitizer for the inorganic oxidizing agent.
Canadian patent 657,242 discloses the use of a heated solution in combin1ng the ammonium ni~rate into the explosive composition. Canadian patent 657,934 requires the use of a ~iinely divided ammonium nitrate with a~
liquifiable carbon such as fuel oil. Canadian p~tent 713,491 uses a surfactant in combination with nitric acid where the fuel material is essentially unreactive with the nitric acid component to provide a s~able composition. Canadian patent 829,23Q discloses the use of hexamethylene triamine~sensitizers for an ammonium nitrate explosive composition.
With the e~plosive compositions~disclosed in these patents, no attention has been directed to the mixing technique and as experience in the marketplace, these ~ ~.
:, :
composlti.ons are routinely mixed in various orms o~
rotatiny blade mixers ancl stirrers which are operated at a constant speed oE mix:i.ng.
The method, apparatus and aqueous slurry explosive mixture in accordance with this invention provides a composition which has improved performance, is economical to manufacture and the apparatus is particularly compact lending itself for use as a mobile unit.
SUMMARY OF THE INVENTION
.
According to an aspect of the invention, the apparatus mixes on a batch basis components of an aqueous sl.urry explosive mixture comprising:
i) 8~ to 25~ by weight water;
ii) 50% to 85~ by weight of an inorganic oxidizing salt selected from the group consisting of ammonium nitrate, alkali metal and alkaline earth metal nitrates and perchlorates, ammonium perchlorate and mixtures thereof;
iii) 2~ to 10% by weight of an organic liquid selected from the group consisting of ethylene glycol, propylene glycol, diethylene glycol, formamide, fuel oil, mineral oils and their emulsions and mixtures thereof, iv) 3~ to 15% by weight of an organic solid selected from the group consisting of sugar, hexamine, finely ground coal, sawdust, and pine needles and mixtuxes thereof, v) 0% to 6% by weight of air entraining agents selected from the group consisting of glass, Saran (trademark) or borate microspheresj perlite, ~ :
vermiculite, paint grade aluminum, milled aluminum, silicon, ferrosillcone, frothing aqents and mixtures thereof, : ~ :
vi) 0~ to 25~:by weight of densifying agents selected from the group consisting of barlte, magnetite, : hot ammonium nitrate solutions and mixtures `~ thereof, .
.
vii) 1% to 4% hy weight of thickening agents selected from the group consisting of flours, gumæ and mixtures thereof, viii) 0% to 25% by weight of ancillary components selected from the group consisting of catalysts, pH
adjusters and a self-explosive.
The improvement in the apparatus comprises a variable speed rotary mixer in which explosive components, as added to the mixer, are mixed at various rotational speeds which are predetermined by the sequence of addition of components.
The use of this type of mixer in formulating batches of explosive compositions lends itself to use on a mobile unit. This arrangement, therafore, avoids preparation of the compositions at the plant and ready use in the field to avoid the problems with transportation of the prepared materials from the plant to the field. Accordingly, the invention provides a mobile mixing plant for mixing on a batch basis components of an aqueous slurry explosive mixture. The mobile plant comprises a plurality of storage tanks for individual components to be mixed. A rotary mixer mixes the components. Each storage tan~ has means for transferring a batch quantity of the respective explosive slurry component to the mixer. A variable speed drive rotates the mixer. Means is provided for controlling the variable speed drive to rotate the mixer at various rotational speeds which are predetermined by~
~ 30 ths sequence of addition of the components to the mixer.
~11 of the individual components introduced to the mixer remain in the mixer until completely mixed by the rotary mixer into an aqueous slurry explosive mixture. Means is provided for withdrawing the aqueous slurry explosive mixture from the mixer.
According to another aspect of the invention, the method for preparing the explosive composition comprises mixing at a first speed in the mixer 10 to 20 parts by weight of ambient temperature water with 3 to 12 parts by weight of sugar and 9 to 5 parts by weight of an air ;
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bubble entraining agent other than paint fine aluminum.
Mixing is continued at this ~irst speed and 50 to 85 parts by weight of ground ammonium nitrate is added.
After addition the mixing speed is increased to a second speed in forming a saturated solution o~ ammonium nitrate. At this second speed, 0 to 5 parts by weight of paint fine aluminum in a plastic mesh binding is - mixed. A dispersion of 1 to 4 parts by weight of guar gums and 2 to 6 parts by weight of ethylene glycol is added and mixing continued at the second speed. The mixing speed is reduced to the first speed when complete distribution of the components is achieved and mixing is continued at the first speed until the guar gum content is completely hydrated.
BRIEF DESCRIPTION OF DRAWINGS
Preferred embodiments of tha invention are shown in the drawings wherein:
Figure 1 is a schematic of the apparatus according to this invention adapted for use as a mobile unit.
DETAILED DESCRIPTION OF TH~ PREFERRED EMBODIMENTS
The apparatus, according to this invention, is adapted for use in mixing small batches of up to 5,000 pounds of aqueous slurry explosive mixtures. The batches are of a size such that, when mixed by the apparatus of this invention, a homogeneous consistent explosive mixture with reliable performance is produced.
The apparatus 10, as shown in Figure 1, is adapted for use on a mobile unit 12 having truck cab 14 and flat bed 16. The apparatus 10 is secured to the flat bed 16 where the rotary mixer 18 is supported on the flat bed 16 by posts 20 and 22~ The mixer 18, according to this preferred embodiment, is a double ribbon rotary mixer having a tank 24 which is semi-circular in cross-section along its bottom 26. According to an embodiment of the invention, the tank 24 may be cylindri¢al where the end walls 28 and 30 are upright and planar. The shaft 32 for the mixer is bearingly mounted in the walls by bearings 34 where the shaft extends outwardly~of end wall 28 to be driven by motor 36. Secured to the shaft is an outer helical ribbon bar 38 which is connected to , `:
: '' ` :
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the shaft by radial arms 40. I'he outer helical ribbon bar extends along ancl is symmetrical about the shaft.
Similarly, an inner ribbon bar 42 is secured to the shaft by shorter arms 44 and extends along ancl is symmetrical about the shaft. The outer helical ribbon bar 38 extends alony the tank in a first rotational direction and the inner helical ribbon bar 42 extends along the tank in a second rotational direction opposite to that of the first rotational direction. This arrangement for the double ribbon mixer bars induces a forward and a reverse flow to the mixture in providing continuous shear blending oE the mixture components.
According to a preferred embodiment of this invention, there are two sets of the inner and outer helical ribbon bars in the double ribbon mixer blender 18. It is appreciated that other types of mixers may be used with the variable speed feature of this invention for mixer explosives. Other types of mixers include blade type and paddle type.
Preferably the bottom portion 26 of the mixer tank 24 is sloped towards the outlet 46 which has a control valve 48 for passage of the mix components via conduit 50 to pump 52. It is appreciated that other forms of rotary mixers may be used,~such as rotary paddle mixers, blade mixers and the like. The important aspect of these mixers is that they have variable speed facility.
The components for the aqueous slurry explosive mixture are stored in storage tanks 54, 56, 58, 60 and 62. The mixed product, when taken off the mixing tank 24, is pumped by pump 52 into the slurry explosive ;
mixture storage tank 64. It is appreciated that the storage tank 64 is optional in that the mixture when taken off the mixing tank 24 may be pumped directly via ~ hose~66 into the bore holes.~ ~
- ~ Storage tank 54 stores the ammomium nitrate 68 whi~h is ground by a stainless steel hammer mill 70.
The ground material falls onto the base 72 of auger 74 which is driven by hydraulic motor 76. The ground ammomium nitrate is augered up to inlet 78 for ., - ' ~2~
introduction to within the mixing tank 724. The microspheres 80 are stored in tank 56 and a quantity thereof is introduced to the mixiny tank 24 via conduit 82 as controlled by valve 84. Storage tank 58 is for the thickening agents which may be guar gum and ethylene glycol. These components are mixed by stirrer 86 which is driven by hydraulic motor 88. ~he mixed thickening agents are introduced to the mixing tank via conduit 90 as controlled by valve 92~
Storage tank 60 may be used as the water metering tank containing ambient temperature water 94. A site glass may be provided on the side of the tank to indicate the quantity of water being dispensed via conduit 96 into the mixing tank as controlled by control valve 98~ The storage tank 62 may be used to store the batch weight of sugar 100 which is dispensed via conduit 102 into the mixing tank as controlled by control valve 104.
In addition to hydraulic motors 36, 76, 88, hydraulic motors ara also provided for driving pump 52 and a pump (not shown) in the hose reel 67. For each hydraulic motor is a set of lines such as 106 and 108 for hydraulic motor 76. A cont:rol device 110 is provided for controlling the flow of pressurized hydraulic fluid in the linas 106, 108 to the various motors. The pressurized hydraulic fluid may be provided to the controller 110 by way of a hydraulic pump mounted on a power take of~ from the engine compartment 112 of the mobile unit. By way of a manifold arrangement, the pressurized fluid may be distributed tG the various lines 106, 108 for each of the hydraulic motors as determined by the controller 110. Switches 114 and 116 are provided for the motors on pump 52 and the pump within the hose reel 67. Since these pumps are not of variable speed, simple on/off switches are all that is required. For hydraulic motor 36, rotary valve 118 is provided to control the ~low rate of the hydraulic fluid in the lines ~06, 108 to motor 36, where by calibration the speed at which the shaft 32 is turning is read out ~3 on meter 120. Similarly, control valve 122 in combination with meter 124 determines and indicates the speed of the motor 88 for the stirrer 86. The hydraulic motor 76 is controlled by variable control valve 126 where its speed is indicated on meter 128.
In accordance with the sequence of additions of the various components for the explosive mixture, the speed at which the rotary mixer 18 is driven is determined by the control valve 118, the details of which will be explained with respect to Examples demonstrating the mixing of preferred compositions. The controller 110 is set up to provide a ranye of mixing speeds in the rotary mixer varying from approximately 20 rpm to approximate.ly 100 rpm.
It is appreciated that in the pumping arrangement to economize on the number of pumps used in handling the slurried explosive, the conduit and valving arrangement may be modified so that pump 52 may be used to not only transfer the mixed slur~y composition into storage tank 64, but also be used to withdraw the explosive mixture from the tank 64 via outlet conduit 130 and pump it ~; through the hose 66 thereby eliminating the pump and the hose reel 67. This may be accomplished by rerouting conduit 130 to the inlet 50 of pump 52 and providing a T-section on the outlet of pump 52 where, in addition to conduit 132 which transfers the mixed slurry to the storage tank 64, there is a second conduit which is interconnected to the hose reel 67.
The apparatus, according to this invention, is useful in preparing many forms of aqueous slurry explosive mixtures. In general, the apparatus according to this invention may be used to mix explosive mixtures which have the following composition:
i) 8~ to 25% by weight water;
ii) 50% to 85~ by weight of an inorganic oxidizing salt selected from the group consisting of ammonium nitrate, alkali metal and alkaline earth metal nitrates and perchlorates, ammonium perchlorate and mixtures thereof;
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iii) 2~ to 10% by weight of an organic liquid selected ~rom the grollp consisting of ethylene ylycol, propylene glycol, cliethylene ylycol, formamide, Euel oil, mineral oils and their emulsions and mixtures thereof, iv) 3% to 15% by weight of an oryanic solid selected from the group consisting of sugar, hexamine, finely ground coal, sawdust, and pine needles and mixtures thereof, v) 0% to 6% by weight of air entraining agents selected from the group consisting of glass, Saran (trademark) or borate microspheres, perlite, vermiculite, paint grade aluminum, milled aluminum, silicon, ferrosilicone, frothing agents and mixtures thereof, vi) 0% to 25% by weight of densifying agents selected from the group consisting of barite, magnetite, hot ammonium nitrate solutions and mixtures thereof, vii~ 1~ to 4% by weight of thickening agents selected from the group consisting of flours, gums and mixtures thereof, viii) 0~ to 25% by weight of ancillary components selected from the group consisting of catalysts, pH adjusters and a self-explosi~e.~
Th.is product may be either packaged for later loading or pumped in bulk form down blast holes.
Conventional priming devices, such as blasting caps,; ~ ;
cast primers or detonating cord, may be used to initiate these products with exceptional and reproducable :
results. The priming devices may be of the well known variety used, such as PETN (pentaerythritol tetranitrate), TNT, RDX (cyclotrimethylenetrinitra amine), Tetryl or the like. ~ ; ~
The inorganic oxidiæing component includes nitrate fertilizers in prill form, particulated form and in solution. These nitrate fertilizer mixtures may include ammonium nitrate, sodium nitrate, calcium nitrate, and other metal nitrates. Also perchlorates or , :. : :
.
:~
pe~manganates of ammonia. The blending of the ammonium nitrates and the like in the slurry composition i~
conducted with cold wa-ter, that is water at a~bient temperature. There is no neecl to heat the wa~er used in the system in forming the saturated solution ~or the ammonium nitrate mixture. Normally the water is at 40F
and thereby forming a saturated solution at this temperature, where normally the temperature does not exceed this level. In so doing, we do not ~orm crystals in the slurry as compared to systems which may use hot water in dissolving the ammonium nitrate which upon cooling can form growth masses of insensitive ammonium nitrate crystals, thereby affecting the reproducibility of the blasting power of the composition Various fuels are used which may include glycol f sugar, carbon commuted to -30 mesh, fuel oil, hexamines and formamide. It is understood that the term sugar covers any form of suitable sugar substance, such as standard granular sucrose, dextrose and the like which can be used in an explosive mixture as a carbon source.
Explosives may be used such as TNT, PETN, or fine grained smokeless powders. Metals such as aluminum, silicon, ferrosilicon; metal oxides such as barite or magnetite may be included as fuels or densifying agents.
Emulsifiers may be required to suspend certain liquid fuels.
Since heat transfers within the explosive is assisted by adiabetic compression of the micro air bubbles, inclusion and distribution of these ~ubbles lS
preferable to ensure detonation with no self-explosive in the slurry composition. Suitable agents for incorporating micro air bubbles are frothers, such~as Deriphat (trademark), micro balloons, such as made from Saran ~trademark), glass or borates and low density metals which have been rolled to entrap air while being ground, such as certain aluminum powders commonly known ~ as paint fine aluminum.
; To provide long term storage in either package form or down the bore hole bulk form, guar gum is , ll l Z~J~
selected optionally containing suitable catalysts. The mixture iB kept at suitable pH with appropriate bufEering agents, such as ammonium hydroxide or nitric acid until the final point of use. A parid pH change may be induced by ammonium gas solution, nitric acid mixtures or sodium dichromate solution. This creates a final product known as a gel which is water reslstant and thus very useful in bore hole applications.
~he apparatus 10, as used in mixing the slurry, may have premeasured amounts of each of the components for the mixture, so that the exact amount in each of the storage tanks 54, 56, 58 60, and 62 are introduced to the mixing tank 24. In the alternative, where smaller batches of explosive are required, various types of metering and weighing devices (not shown) may be used so that the axact proportions of the mixture components can be introduced to the mixing tank 24 for mixing. It is appreciated, of course, that the mixing tank 24 will have upper and lower limits in terms of the amount for each batch to be mixed. Preferably in mobile units, the mixing tank 24 is of a size that will handle ranges in batch compositions of 500 to 5000 lbs.
An aqueous slurry explosive of the following composition range is made up as follows:
i~ 10% to 20% by weight of water, ii) 3% to 13% by weight of sugar, iii) 1% to 5~ by weight of an air entraining agent selected from the group consisting of borate microspheres, glass microspheres, Saran microspheres and milled aluminum of 5 to 20 ~ particle size, iv) 50% to 85% by weight of ammonium nitrate, v~ 2% to 6% by weight of ethylene glycol, vi) 1% to 4% by weight of guar gums, vii) 0% to 15% by weight of ground aluminum as a th~rmal energy additive.
Based on 100 parts by weight, the following specific composition was mixed: 13 part~ by weight of water was introduced to the mixer, then 10 parts by weight of . ~.
.. : - ' '` 1~
sugar and 2 parts by weighk of Q-cells ( trademark) (microspheres oE tiny hollow part.icles that encapsulate air in a spherical shell) we,re added to the mixer and blended completely for approximately 2 minutes at a speed of 40 rpm. Seventy-two parts by weight of crushed ammonium nitrate was added while blending at 40 rpm.
When all ammonium nitrate was added, the mixer speed was increased to 80 rpm for 2 minutes.
One part by weight and 2 parts by weight of guar gums and glycol were mixed in the stirrer storage tank 58 and introduced to the mixer which continued mixing at 80 rpm. When complete distribution was achieved, the mixer speed was lowered to 40 rpm until the guar gums were completely hydrated. The composition was then ready for transfer to the bore holes or storage in the storage tank 64.
It has been found that the explosive composition is particularly inexpensive to manufacture and has a good explosive property. The following table compares the power of the above specific composition to known materials, POWER OF SUGAL GEL
Weight Energy Bulk Energy~ Density Product Kilocalories/Gram Kilocalories/cc GMS/cc _ _ ~ . ~ _ ANFO 0.84 0.69 0.83 (Ammonium Nitrate Y
Fuel oil 30 Explosive ~ ~ ~
Standard 0.7972 ~ 1.1161 1.40 TNT Slurry ~ ~ ~
Specific 0.6298 0.7872 1~25 Mix of this Invention ~ ........ ,.. 0.. _~.. _ I
Production blasting confirmed that the product without aluminum additives compares favourably to ANFO
on a bulk energy basis. As with all water gels, :
~",.
,~
aluminum Euels may be used to add linearly to the power.
Fuel grade aluminum may be used in these compositions to provide higher strengths. Up to a level of approximately 15~ by weight oE aluminum may be used.
The fuel yrade aluminum is usually through -30 mesh and retained on a ~100 mesh screen. The paint fine aluminum in a ~eflon mesh is added to the mixture at the higher mixer speed of 80 rpm. This higher speed properly dispenses the aluminum fines throughout the mixture.
The variable speed rotary mixer is particularly useful in blending the microspheres without breakage.
Equal utility is ~ound in dispensing paint fine aluminum which has the "Teflon" (trade mark of Dupont for a fluorocarbon resin) mesh bonding the aluminum fines.
This does not disperse properly during normal mixing.
However in using the double ribbon blender at variable speeds, the desired mixing is achieved in forming a uniform dispersion of the aluminum fines through the mix without wetting the aluminum and thereby driving off the micro air bubbles trapped on the aluminum fines during milling. Because of the efficiency of the mixer, a compact arrangement is provided for ~he apparatus which lends itself readily for use on mobile units. Thus the unit may be driven to the field with the components unmixed, thereby avoiding segregation of premixed components. The system~may then prepare the desired amount of explosive composition for dispersal through the hose 66 to the various bore holes in the material to be blasted. Also because of its compactness, the apparatus may be used in underground mines to ensure balancing of the oxidizing components so that poisonous gases ater an explosion are Xept to a minim~m. This~is accomplished by ensuring an oxygen balance in the composition as prepared with the components uni~ormly dispersed throughout the mixture by the mixer.
Although preferred embodiments of the invention have been described herein in detail, it will be understood by those skilled in the art that variations ~,~
,~
1~
may be made thereto wlthout departing frorn the spirit of the invention or the scope o~ the appended claims.
: :
~:
~ ~
. :
Claims (19)
PRIVILEGE IS CLAIMED ARE DEFINED AS FOLLOWS:
1 In an apparatus for mixing on a batch basis components of an aqueous slurry explosive mixture comprising:
i) 8% to 25% by weight water;
ii) 50% to 85% by weight of an inorganic oxidizing salt selected from the group consisting of ammonium nitrate, alkali metal and alkaline earth metal nitrates and perchlorates, ammonium perchlorate and mixtures thereof;
iii) 2% to 10% by weight of an organic liquid selected from the group consisting of ethylene glycol, propylene glycol, diethylene glycol, formamide, fuel oil, mineral oils and their emulsions and mixtures thereof, iv) 3% to 15% by weight of an organic solid selected from the group consisting of sugar, hexamine,finely ground coal, sawdust, and pine needles and mixtures thereof, v) 0% to 6% by weight of air entraining agents selected from the group consisting of glass, Saran or borate microspheres, perlite, vermiculite, paint grade aluminum, milled aluminum, silicon, ferrosilicone, frothing agents and mixtures thereof, vi) 0% to 25% by weight of densifying agents selected from the group consisting of barite, magnetite, hot ammonium nitrate solutions and mixtures thereof, vii) 1% to 4% by weight of thickening agents selected from the group consisting of flours, gums and mixtures thereof, viii)0% to 25% by weight of ancillary components selected from the group consisting of catalysts, pH adjusters and a self-explosive;
the improvement comprising a variable speed rotary mixer in which components as added to said mixer are mixed at various rotational speeds which are predetermined by the sequence of addition of said components.
i) 8% to 25% by weight water;
ii) 50% to 85% by weight of an inorganic oxidizing salt selected from the group consisting of ammonium nitrate, alkali metal and alkaline earth metal nitrates and perchlorates, ammonium perchlorate and mixtures thereof;
iii) 2% to 10% by weight of an organic liquid selected from the group consisting of ethylene glycol, propylene glycol, diethylene glycol, formamide, fuel oil, mineral oils and their emulsions and mixtures thereof, iv) 3% to 15% by weight of an organic solid selected from the group consisting of sugar, hexamine,finely ground coal, sawdust, and pine needles and mixtures thereof, v) 0% to 6% by weight of air entraining agents selected from the group consisting of glass, Saran or borate microspheres, perlite, vermiculite, paint grade aluminum, milled aluminum, silicon, ferrosilicone, frothing agents and mixtures thereof, vi) 0% to 25% by weight of densifying agents selected from the group consisting of barite, magnetite, hot ammonium nitrate solutions and mixtures thereof, vii) 1% to 4% by weight of thickening agents selected from the group consisting of flours, gums and mixtures thereof, viii)0% to 25% by weight of ancillary components selected from the group consisting of catalysts, pH adjusters and a self-explosive;
the improvement comprising a variable speed rotary mixer in which components as added to said mixer are mixed at various rotational speeds which are predetermined by the sequence of addition of said components.
2. In an apparatus of claim 1 said mixer being a double ribbon mixer.
3. In an apparatus of claim 2, said double ribbon mixer comprises an elongate mixing tank with a semi-circular bottom and upright end walls, a shaft extending the length of said mixer and bearingly mounted for rotation in said end walls, said shaft being coincident with the centre of curvature of said semi-circular bottom, said double ribbon comprising an inner helical ribbon bar extending along and symmetrical about said shaft and an outlet helical ribbon bar extending along and symmetrical about said shaft, said outer helical ribbon bar extending along said tank in a first rotational direction and said inner helical ribbon bar extending along said tank in a second rotational direction opposite to said first rotational direction, a variable speed drive for rotating said shaft, and means for controlling said variable speed drive to rotate said shaft at any rotational speed selected from the range of rotational speeds provided by said variable speed drive.
4. In an apparatus of claim 2, said double ribbon mixer induces a forward and a reverse flow to said mixture in providing continuous shear blending of the mixture components.
5. In an apparatus of claim 2, 3 or 4, said variable speed rotary mixer providing a range of mixing speeds from approximately 20 rpm up to approximately 100 rpm.
6. In an apparatus of claim 2, 3, or 4, means for withdrawing from the bottom of said tank said batch after the components are mixed.
7. In an apparatus of claim 1, said rotary mixer tank having a capacity for mixing up to a 5000 pound batch of a slurry explosive mixture.
8. A mobile mixing plant for mixing on a batch basis components of an aqueous slurry explosive mixture, said mobile plant comprising a plurality of storage tanks for such individual components to be mixed, a rotary mixer for mixing such components, each storage tank having means for transferring a batch quantity of the respective slurry component to said mixer, a variable speed drive for rotating said mixer, means for controlling said variable speed drive to rotate said mixer at various rotational speeds which are predetermined by the sequence of addition of said components to said mixer, all of said individual components introduced to said mixer remaining in said mixer until completely mixed by said rotary mixer into an aqueous slurry explosive mixture and means for withdrawing such aqueous slurry explosive mixture from said mixer.
9. A mobile mixing plant of claim 8, wherein said mixer is a double ribbon mixer.
10. A mobile mixing plant of claim 9, wherein said double ribbon mixer induces a forward and a reverse flow to said mixture in providing continuous shear blending of the mixture components.
11. A mobile mixing plant of claim 9, wherein said double ribbon mixer comprises an elongate mixing tank with a semi-circular bottom and upright end walls, a shaft extending the length of said mixer and bearingly mounted for rotation in said end walls, said double ribbon comprising an inner helical ribbon bar connected to said shaft and extending along and symmetrical about said shaft and an outer helical ribbon bar connected to said shaft and extending along and symmetrical about said shaft, said outer helical ribbon bar extending along said tank in a first rotational direction and said inner helical ribbon bar extending along said tank in a second rotational direction opposite to said first rotational direction.
12. A mobile mixing plant of claim 8, 9 or 10, wherein said mixer has a capacity for mixing up to a 5000 pound batch of a slurry explosive mixture.
13. A mobile mixing plant of claim 10, wherein said means for withdrawing the mixed batch of aqueous slurry explosive from said mixer transfers said slurry explosive mixture to a product storage tank, means for dispensing said slurry mixture from said storage into bore holes of material to be blasted by the explosive mixture.
14. A mobile mixing plant of claim 10, 11 or 12, wherein said mixing tank has a capacity mixing up to a 5000 pound batch of a slurry explosive mixture, a pump in combination with valving arrangement transfers said mixed slurry explosive to said storage tank and dispenses via a hose said mixed slurry explosives from said product storage tank.
15. A mobile mixing plant of claim 8, wherein said variable speed drive is a hydraulic motor and said control means controls the rate of flow of pressurized hydraulic fluid to said motor to provide infinite variable speed settings for said mixer.
16. A mobile mixing plant of claim 9 or 14, wherein said control means provides a range of mixing speeds from approximately 20 rpm up to approximately 100 rpm.
17. A method of mixing a batch of aqueous slurry explosive comprising mixing 100 parts by weight of components of said slurry explosive in a variable speed mixer which induces a forward and a reverse flow to said mixture in providing continuous shear blending of the mixture components, said method comprising mixing at a first speed in said mixer 10 to 20 parts by weight of ambient temperature water with 3 to 12 parts by weight of sugar and optionally up to 5 parts by weight of air bubble entraining agent other than paint fine aluminum, continue mixing at said first speed and adding 50 to 85 parts by weight of ground ammonium nitrate and increasing the mixing speed to a second speed in forming a slurry of ammonium nitrate, adding if needed up to 5 parts by weight of paint fine aluminum air bubble entraining agent in a plastic mesh binding to provide a total of said air bubble entraining agent up to approximately 6 parts by weight, adding a dispersion of 1 to 4 parts by weight of guar gums and 2 to 6 parts by weight of ethylene glycol and continuing mixing at said higher second speed, reducing mixing speed to said first speed when complete distribution of components is achieved and continuing mixing at said first speed until the guar gum component is completely hydrated.
18. A method of claim 17, wherein said first speed is approximately 40 rpm and said second speed is approximately 80 rpm.
19. A method of claim 17, wherein said air bubble entraining agent is selected from the group consisting of milled aluminum, glass microspheres, plastic microspheres, borate microspheres and mixtures thereof.
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CA000453746A CA1244244A (en) | 1984-05-07 | 1984-05-07 | Mix-delivery system for explosives |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CA000453746A CA1244244A (en) | 1984-05-07 | 1984-05-07 | Mix-delivery system for explosives |
Publications (1)
| Publication Number | Publication Date |
|---|---|
| CA1244244A true CA1244244A (en) | 1988-11-08 |
Family
ID=4127816
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| CA000453746A Expired CA1244244A (en) | 1984-05-07 | 1984-05-07 | Mix-delivery system for explosives |
Country Status (1)
| Country | Link |
|---|---|
| CA (1) | CA1244244A (en) |
Cited By (4)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| EP0659528A1 (en) * | 1990-05-24 | 1995-06-28 | Trw Vehicle Safety Systems Inc. | Spheronizing process |
| WO1997024298A1 (en) * | 1995-12-29 | 1997-07-10 | Orica Australia Pty Ltd | Process and apparatus for the manufacture of emulsion explosive compositions |
| US6539870B1 (en) | 2000-11-22 | 2003-04-01 | Dyno Nobel Inc. | Blasting method for reducing nitrogen oxide fumes |
| CN118050363A (en) * | 2024-04-16 | 2024-05-17 | 宁德时代新能源科技股份有限公司 | Detection method and detection device |
-
1984
- 1984-05-07 CA CA000453746A patent/CA1244244A/en not_active Expired
Cited By (5)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| EP0659528A1 (en) * | 1990-05-24 | 1995-06-28 | Trw Vehicle Safety Systems Inc. | Spheronizing process |
| WO1997024298A1 (en) * | 1995-12-29 | 1997-07-10 | Orica Australia Pty Ltd | Process and apparatus for the manufacture of emulsion explosive compositions |
| US6165297A (en) * | 1995-12-29 | 2000-12-26 | Orica Australia Pty Ltd | Process and apparatus for the manufacture of emulsion explosive compositions |
| US6539870B1 (en) | 2000-11-22 | 2003-04-01 | Dyno Nobel Inc. | Blasting method for reducing nitrogen oxide fumes |
| CN118050363A (en) * | 2024-04-16 | 2024-05-17 | 宁德时代新能源科技股份有限公司 | Detection method and detection device |
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