CN85101581A - Emulsion explosive composition - Google Patents
Emulsion explosive composition Download PDFInfo
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- CN85101581A CN85101581A CN85101581.6A CN85101581A CN85101581A CN 85101581 A CN85101581 A CN 85101581A CN 85101581 A CN85101581 A CN 85101581A CN 85101581 A CN85101581 A CN 85101581A
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Abstract
A kind of emulsion explosive composition that contains discontinuous phase that oxygen-supplying component is arranged and the organic medium that forms external phase, wherein oxygen-supplying component and organic medium can form latex.Do not having to be no more than 60000 slight ohm/meter in 60 ℃ of specific conductivity that record this latex under the auxiliary that replenishes.Such specific conductivity can reach by adding modifying agent.The mixture storge quality improves.
Description
The invention relates to a kind of pyrotechnic composition, especially a kind of invention of emulsion explosive composition.Such emulsion explosive composition contains a discontinuous oxygenant phase, it be dispersed in fully one basically with its immiscible continuous fuel mutually in.
Commercial available emulsion explosive composition generally contains a foreign minister or continuous organic-fuel phase, a kind of oxygen source water liquid dispersed droplets is arranged as interior phase or discontinuous phase among the foreign minister.The emulsion explosive composition of the so-called water of this pyrotechnic composition in oil, the example have obtained explanation, especially at United States Patent (USP) 3447978,3674578, have obtained explanation in 3770522,4104092,4111727,4149916 and 4149917.
With regard to some application, the emulsion explosive oxygenant mutually may be not moisture fully or be dropped to a low scope to major general's water content, for example is brought down below 4% of latex mixture gross weight.Such mixture is commonly referred to as melt in oil or the emulsion explosive of melt in fuel, and has obtained explanation, has obtained explanation especially in United States Patent (USP) 4248644.
" emulsion explosive composition " speech is used to comprise water (fuel) and melt pyrotechnic composition of (fuel) two types in oil in oil hereinafter.
Generally, in the presence of surface tension improvement emulsifying agent, form emulsion explosive composition, select for use this improvement emulsifying agent with the segmentation of promotes oxidn agent phase droplet and impel it to be scattered in the external phase.In addition, emulsifying agent is considered to exist in the lip-deep molecular coatings of droplet as a kind of, thereby, by stoping the gathering and the agglomerating initial destruction of reducing latex of droplet.
Oxygenant phase droplet usually is metastable state and shows a kind of crystallization tendency.The crystalline growth that is generated helps to weaken the emulsion explosive composition detonation sensitivity, and along with the crystalline matrix that occurs links mixture solidified, thereby the difficulty of detonating.Therefore common emulsion explosive composition shows blast performance usually and reduces gradually, this be because in explosive production and between the shelf lives between using and or the delivery period between the weathering process that produces cause.
The multiple effort that improves the emulsion explosive composition storge quality still concentrates on the mixture emulsifier component so far, is especially selecting on suitable emulsifying agent or its mixture.The gathering of the oxidizer salt supersaturation drop that exists is eliminated in attempt in discontinuous phase with emulsifying agent.Suggestion provides the latex blasting mixture of a kind of water in oil in british patent specification 2042495.This latex blasting mixture contains a kind of organic cation emulsifying agent as unique emulsifying agent, and it has a hydrophilic part and an oleophilic moiety, and the latter is a kind of aliphatic unsaturated hydrocarbon.Fatty acid amine or ammonium salt that this unsaturated emulsifying agent can be a kind of 14 to 22 carbon atom chain lengths it is said the crystalline structure modifying agent of crystalline growth effect in control, the restriction oxidizer salt solution.Yet, such emulsion explosive composition for blast relatively insensitive (to detonator insensitive-for example can not be by magnitude less than No. 8 capsular blasting cap initiations of standard), and, the critical diameter (being lower than it will not detonate with the cartridge bag that this mixture loads) that is about 19mm is arranged when preparation.These mixtures are useful really and have the coml purposes, available it as the explosive agent in the cartridge bag more than the 25mm diameter.Reach applicable purpose when less critical diameter, can only form salt and finish by in mixture, mixing a kind of vast scale low melting eutectics, nitrocalcite for example, its reduces the gas volume that explosion time produces, thereby explosive is had a negative impact.
Employed straight chain hydrocarbon emulsifier component is normally saturated before in producing emulsion explosive composition, but rely on a kind of unsaturated straight chain hydrocarbon to make the emulsifying agent oleophilic moiety at the said mixture of producing according to English Patent 2042495, this explosive is more stable and have a higher sensitivity of explosive that contains saturated hydrocarbon chain than use.Find that in addition unsaturated straight chain hydrocarbon emulsifying agent is at the saturated equivalent that is better than them aspect the prevention oxygenant crystalline growth greatly.
We have designed the responsive emulsion explosive composition of a kind of detonator now, aspect stability in storage, show beyond thought, significant advantage.
Thereby, the invention provides a kind of hole glue pyrotechnic composition that the oxygen-supplying component discontinuous phase arranged and form a kind of organic medium of external phase that contain, oxygen-supplying component and organic medium can form a kind of latex in this explosive, when not replenishing auxiliary, the specific conductivity of this explosive is measured down in 60 ℃ and is no more than 60000 slight ohm/meter.
The present invention further provides a method for preparing emulsion explosive composition, comprised in the method that a kind of oxygen-supplying component of emulsification and an organic medium are to form this step of latex.Oxygen-supplying component constitutes the part of discontinuous phase at least in latex, and organic medium constitutes the part of external phase at least, finishes emulsifying effect therein under the situation that has modifying agent to exist.Modifying agent can reduce the specific conductivity of the latex that is formed by oxygen supply salt component and organic medium, records its value in 60 ℃ and be not higher than 60000 slight ohm/meter under the situation of not adding auxiliary.
By selecting emulsible oxygen-supplying component and organic medium so that it can generate a kind of emulsion explosive composition that low especially specific conductivity is arranged.We observe this pyrotechnic composition can obtain surprising improvement aspect stability in storage.Usually can meet the demands storage time when latex specific conductivity (60 ℃) is no more than 60000 slight ohm/meter, yet explosive shows the specific conductivity that is lower than 20000 slight ohm/meter preferably.A kind of desirable especially emulsion explosive composition has long stability in storage, has the specific conductivity (60 ℃) that is lower than 2000 preferable 200 slight ohm/meter.
For may needing to lead modifying agent just like the electricity of hereinafter setting forth, the specific conductivity that reaches regulation exists.
Emulsion explosive composition will contain a kind of auxiliary usually at least to improve or to improve the performance of explosive.Such auxiliary has the paraffin that improves rheological property, reduces blank agent such as bubble, porous particulate or the microballoon of proportion, plays the like carbon of solia particle shape material or the aluminium of auxiliary fuel composition effect.Such material is influencing specific conductivity size and is covering modifying agent of the present invention probably reducing of any specific conductivity of being caused in varying degrees.Therefore conductivity value used herein is under the situation without any a kind of auxiliary that influences the specific conductivity size, measures on latex mixture.In fact, but for guaranteeing the reproducibility of measuring result, prepared a kind of latex mixture under the following conditions.A kind of solution of vigorous stirring or oxidant constituents disperse phase (moisture usually) are in organic external phase medium in an epicyclic mixer, and at least 70 ℃ of temperature stirred 5 minutes.Emulsification can be finished in the presence of suitable modifying agent.Perhaps modifying agent can be stirred in the latex that has formed.The specific conductivity of resulting latex can be measured in the specific conductivity galvanic cell then.
Galvanic cell has two 304 parallel stainless steel flat plate electrodes, makes it keep the distance (ICI ' C ｀ Perspex ' (trade mark) board is suitable for) of 3mm by the peripheral spacer of poly-methyl methacrylic acid ester.Each electrode has 10cm
2Plane of action, plane of action and each dull and stereotyped back side are connected, it is the conduit of a sinusoidal wave formula, thermal medium (for example hot water) can the pipe internal recycle be 60 ℃ to keep the galvanic cell temperature, temperature is controlled by the suitable thermopair that is contained in the battery lead plate end.
The latex sample is placed down between the electrode in the Tc that is higher than it, and electrode pushes simultaneously to discharge unnecessary latex, and a constant volume is arranged when guaranteeing METHOD FOR CONTINUOUS DETERMINATION with peripheral spacer.Up to recorded 60 ℃ of constant by thermopair, measure with 8050A type Fluke conductivity measurement table in the galvanic cell by the specific conductivity of sample through the conduit circulation for hot-fluid then.
Containing under a kind of emulsion explosive composition situation of auxiliary, can be with method extraction oxidant constituents that is dissolved in suitable solvent and component (for example using fractionated method) that organic medium is extracted with recovery, with from a kind of latex that does not contain auxiliary of new formation, the conductivity measurement that meets the requirements can be realized according to aforementioned technology.
Though the present invention is at the numerical value of this definition specific conductivity one speech for not having to measure in the presence of the auxiliary (for example paraffin, metal particle, microballoon, blank agent or the like), any such auxiliary can be comprised in the mixture of the present invention.
The specific conductivity modifying agent of using according to the present invention wishes also should play emulsifying agent at least to a certain extent.Therefore when using under significant quantity, it should promote the discontinuous phase component to be dispersed in relatively enduringly in the external phase medium.Therefore such modifying agent should be the emulsifying agent of a kind of water (or melt) in oil, and its promotes or is convenient to form latex.Discontinuous phase includes a kind of water liquid (or melt) medium in latex, and external phase comprises a kind of oil or organic medium.Modifying agent comprises that hydrophilic segment and oleophilic moiety are more suitable for this reason, and general modifying agent is strongly oil-wet, just oil or organic medium is showed a kind of high avidity.
The modifying agent oleophilic moiety can be unit molecule or polymer substance, and it should contain a sufficiently long chain structure to give essential emulsifying property.Chain structure should comprise the atom of at least 10 connections, preferable no more than 500 skeleton sequence, and these atoms can be carbon atoms fully, or they can mainly be by the carbon atom that heteroatoms disconnected as oxygen, nitrogen.The ideal oleophilic moiety contains a terminal active group, and like hydroxyl, amino, carboxyl or carboxylic acid anhydride group are to be improved to suitable hydrophilic segment with the oleophylic key.
The oleophilic moiety of preferred type is saturated or unsaturated hydrocarbon chain, for example the hydrocarbon chain that gets from the monoene polymkeric substance that contains 40-500 carbon atom.Suitable polyene comprises the polymkeric substance that gets from the alkene that contains 2-6 carbon atom, especially ethene, propylene, butene-1 and isoprene, yet especially with iso-butylene for well.Oleophilic moiety also can be provided easily by a kind of poly-(alkane (alkene) base) succinyl oxide.These all are commercial available things, and they are to make by carrying out addition reaction between polyene that contains the terminal unsaturation group under the high temperature and the MALEIC ANHYDRIDE.Reaction can be carried out in the presence of optional halogen catalyzer.Typical poly-(iso-butylene) succinyl oxide molecular-weight average is 400-5000.
In the compound of mentioning in the above the succinyl oxide base provide one easily condition the oleophylic hydrocarbon chain is linked specific conductivity modifying agent hydrophilic segment.Will discuss below this problem.
Another kind of useful oleophilic moiety is to get from the polymkeric substance that one or more saturated or unsaturated long-chains (for example can up to 25 carbon atoms)-hydroxyl-first carboxylic acid interesterification obtains, this interesterification can, can be not yet with giving mixing in the thing and carry out (latter plays the chain terminator effect) than one or more no hydroxyl-first carboxylic acid of small part and-hydroxyl-first carboxylic acid.Commercial available 12-oxystearic acid generally contains a spot of stearic acid, and this material for example can give the mixed use easily under the situation that maybe will not mix, and more single functional mass produces a kind of complex carboxylic acid by interesterification.The molecular weight of gained complex acid depends on the ratio of the no hydroxylated material of existence, can from 500 to 5000 wait.The interesterification of-hydroxyl and no hydroxyl-first carbonyl acid can be realized that for example (as dimethylbenzene) heating in a kind of hydrocarbon cosolvent produces interesterification by known technology in the presence of catalyzer (for example tetrabutyl titanate salt).
The interesterification product contains terminal carboxyl(group) in molecule, it provides links condition on the suitable hydrophilic radical with the oleophylic polyester chain.
Modifying agent hydrophilic segment used according to the invention is polar and is advisable to contain an organic radical that the molecular weight of organic radical is no more than 450, and is preferable to be no more than 300, and it is 200 especially good to be no more than.When determining above-mentioned molecular weight, (selectively introduce organic radical) because any influence that ion partly brings and do not take into account as illustrated this ion part hereinafter.Though may use the oligomerisation base for example to contain the oleophilic group that is no more than about 10 repeating units, but organic radical wishes it is monomeric, its molecular weight is in above-mentioned scope.The suitable monomers base can obtain from many alcohol, as glycerol, tetramethylolmethane, Sorbitol Powder or its intramolecular anhydride, for example sorbitan; Obtain diamino-vinyl for example, triamino divinyl and dimethyl amine Propanolamine from amine; Obtain from acid amides, for example 2-hydroxyl Propanolamine; Obtain from alkanolamine, as thanomin or diethanolamine; Also obtain Li such as oxazoline or tetrahydroglyoxaline from heterocycle.Suitable oligomerisation base comprises short chain poly-(oxygen ethene) base (just they contain ethylene oxide reach 10 unit).
The simplest unitary class modifying agent is made up of independent monomer base or the oligomerisation base linked on the oleophilic moiety.
The specific conductivity modifying agent that uses according to the present invention can adopt easily method to make according to the chemical property of the oleophylic of modifying agent, hydrophilic segment.For example oleophilic moiety is poly-(iso-butylene) succsinic acid and hydrophilic segment when being many alcohol or alkanolamine, causes that by heat two components (can also have catalyzer to exist if necessary) together in a suitable solution acid anhydride base and hydroxyl or amino react.If desired, such modifying agent forms and can finish in the original place, for example in organic external phase medium of latex, heats two kinds of components (can give heat if desired) appropriate time under certain temperature.In the monocarboxylic place of oleophilic moiety complex, can cause that similarly hydroxyl or the amino in carboxyl and many alcohol or the alkanolamine reacts.
That as above discussed in the mask body explanation is the same, and modifying agent may be a nonionic, but they also may be anionic properties conversely, for example reacts the material that obtains with the free hydroxyl and a kind of strong acid (for example phosphoric acid) that are present in the nonionic modifying agent.If necessary then with in ammonia or the organic bases and products therefrom.They can be cationic again, for example in the place of hydrophilic segment in conjunction with enter polyamines or heterogeneous ring compound base.
Though can use the mixture of two or more modifying agents, mixture of the present invention if necessary also can contain the one-component modifying agent.Modifying agent can be blended in the emulsification with general method and go.
General needs a spot of modifying agent in the mixture of the present invention.The amount of required modifying agent can determine that generally in 0.1% to 5.0% scope of explosive composition total amount, 0.2 to 4.0% is more excellent for the discovery aequum easily by simple test, and 0.5% to 2.5% is especially good.
So far, the emulsifying agent that uses in the preparation emulsion explosive composition is water (or melt) type (like illustrate before this same) in oil normally, generally shows to be lower than about 10 hydrophile-lyophile balance (HLB).At the such emulsifying agent of this explanation is common emulsifying agent.One or more such emulsifying agents can (but be not must) be added in emulsion explosive composition preparation of the present invention with one or more modifying agents if necessary.Yet, when not having common emulsifying agent, also be easy to the preparation emulsion explosive composition that hits pay dirk, and obtain qualified stability in storage.
Many suitable common emulsifying agents describe in detail in the literature, for example, comprise sorbitan ester, like sorbitan sesquialter oleate, sorbitan list oleate, sorbitan list palmitate, sorbitan Monostearate and sorbitan three stearate; Constitute one and two R-Glyceric acid of the lipid acid of fat, sorbitan Yelkin TTS and lanolin derivative such as lanolin fatty acid propyl alcohol ester, the mixture of high molecular Fatty Alcohol(C12-C14 and C12-C18) and wax ester; Hydroxyethylated lipid acid ether, as polyoxyethylene (4) lauryl ether, polyoxyethylene (2) oleic acid base ether, polyoxyethylene (2) stearyl ether, polyoxy alkylene oleyl alcohol laurate and Bao are with De oxazoline such as 2-oleyl alcohol-4,4 '-two (methylol)-2-oxazoline.More than these common emulsifying agent suitable mixture also can be selected in the mixture of the present invention with one or more modifying agents.
Required common emulsification dosage can easily be determined with simple test.But the content of general modifying agent and common emulsifying agent should be greater than about 5% of explosive composition gross weight.Can allow emulsifying agent and/or modifying agent that higher ratio is arranged, unnecessary amount is as the postcombustion of mixture.But usually remain on explosive required minimum content ratio when having acceptable performance from the amount of considering to require emulsifying agent and/or modifying agent economically.
The discontinuous phase oxygen-supplying component contains the oxidizer salt of possibility oxygen release under explosion environment, and its content and oxygen release speed should be enough, so that give latex mixture qualified blast characteristics.Usually the inorganic salt that use in the preparation of emulsion explosive composition and can be used in the mixture of the present invention are disclosed (for example in United States Patent (USP) 3447978), these inorganic salt comprise ammonium salt and basic metal, alkaline earth salt, for example nitrate, oxymuriate and perchlorate and composition thereof.Other suitable salt comprises hydrazine nitrate and crosses the chloric acid urea.Oxygen-supplying component also can comprise a kind of acid such as nitric acid.
Ammonium nitrate is better as oxidizer salt, and content is 50% of oxygen supply salt composition weight at least.If necessary, replenish with a kind of more a spot of (being no more than weight 50%) secondary oxidizer component (for example nitrocalcite or SODIUMNITRATE).The secondary oxidizer component can be added in a kind of moisture discontinuous phase.If but oxygen-supplying component has been added latex with melt form, just do not have by the next water of discontinuous phase substantially or fully, the existence of secondary oxidizer component then is desirable especially.The suitable secondary oxidizer component that generates eutectic melt when heating with ammonium nitrate comprises aforesaid inorganic oxidant salt, for example lead nitrate, Silver Nitrate, SODIUMNITRATE and nitrocalcite; Also include list and the polyol of organic compounds as comprising methyl alcohol, ethylene glycol, glycerol, mannitol, Sorbitol Powder, tetramethylolmethane; Hydrocarbon polymer such as glucose, sucrose, fructose and maltose; Aliphatic carboxylic acid and their derivative such as formic acid and ammonium formate; Also comprise for example urea of organic nitrogen compound, ammonium methyl nitrate and hexanaphthene tetramine and composition thereof.
If desired, latex mixture can also contain the solid oxidizing agent component in addition, and for example solid ammonium nitrate or ammonium perchlorate are respectively granular or powdery usually.
Generally, discontinuous phase can be about 20%-97% of emulsion explosive composition gross weight, 30%-95% more generally, more excellent 70%-95%.Discontinuous phase can not have water fully or can contain the water of relatively small amount under melt latex situation, the 2%-30% of mixture total weight for example, and 4%-25% more generally, 8%-18% is then more desirable.
According to emulsion explosive composition of the present invention, the organic medium that may form external phase plays the effect of pyrotechnic composition fuel, and should be insoluble to the discontinuous phase component basically.Fuel should form latex with the discontinuous phase component when suitable emulsifying agent exists under significant quantity.The emulsive difficulty or ease especially depend on the viscosity of organic medium, though the latex of gained can have one to be solid external phase basically, organic should be able to the beginning just is in enough flow states.If essential, could be by suitable temperature regulation so that emulsification would take place in it.
Form under the temperature of latex being convenient to, be in liquid suitable organic medium and comprise saturated and undersaturated chain hydrocarbon and aromatic hydrocarbons and composition thereof.More excellent medium comprises refining (in vain) mineral oil, diesel oil, paraffin oil, petroleum cuts, benzene, toluene, dinitrotoluene (DNT), vinylbenzene dimethylbenzene and composition thereof.
External phase can contain a kind of wax selectively with the Controlling System rheological except that the organic-fuel medium, though the existence of wax is not absolutely necessary to reaching required specific conductivity.Suitable wax comprises petroleum wax, mineral wax, animal wax and desinsection wax.The fusing point of wax with more than 30 ℃ better and should be compatible easily with formed latex.The fusing point of wax is being good in about 40 ℃ to 75 ℃ scopes.
Usually external phase (comprising wax if there is wax to exist) contains the 1% to 10%(2% to 8% more excellent of pyrotechnic composition total amount), but also can allow higher ratio, for example from 1% to 15% or even 20%.
If desired, annexing ingredient can add in the mixture of the present invention.For example the auxiliary fuel component can be added.The general auxiliary fuel component that is fit to join discontinuous phase comprises soluble carbohydrate, for example glucose, sucrose, fructose, maltose and molasses, low glycols, methane amide, urea element, methylamine nitric ether, urotropin, urotropin nitric ether and other organic nitrates.
The auxiliary fuel that can join external phase comprises lipid acid, higher alcohol, vegetables oil, aliphatic series and aromatic nitro organic compound, dinitrotoluene (DNT) for example, nitric ether, solid particulate matter, for example coal, graphite, carbon, sulphur, aluminium and magnesium in addition.
If necessary, the mixture of said secondary oxidizer component also can use above.
According to the mixture performance demands, use the auxiliary fuel of different amounts.But, generally should be in the emulsion explosive composition gross weight 0 to 30%, 5% to 25% more excellent.
Can comprise thickening material or linking agent in the mixture.If desired, generally from about 10%, 1% to 5% more excellent to the pyrotechnic composition gross weight on a small quantity.General thickening material comprises natural gum, for example protects the glue or derivatives thereof, also comprises synthetic macromolecular compound, especially the synthetic macromolecular compound that gets from propionic acid amide.
More a spot of, nonvolatile, water-fast polymer or elastic material (for example natural rubber, synthetic rubber and polyisobutene) can add external phase.The proper polymer additive comprises butadiene-styrene, isoprene-iso-butylene or iso-butylene-ethylene copolymer.Their trimer also can be used to improve external phase, especially improves the maintenance of the occluded gas in mixture.
Emulsion explosive composition of the present invention (drops to and is lower than 1.5, drop to from about 0.8 to about 1.4g/Cm with the density that reduces them to contain a Discontinuous gas component
3More excellent) and the sensitivity that increases them for well.Gaseous fraction (being generally air) can add in the mixture of the present invention, as is scattered in the small bubble in the whole mixture, often is called as the hollow bead of microballoon, porous particle or its mixture.The discontinuous phase of micro-bubble can add in the mixture of the present invention with following method: use churned mechanically method; With the gas injection or with the method for blister by mixture; The method of chemical aerogenesis on the spot.The suitable compound that produces bubble on the spot comprises superoxide (for example hydrogen peroxide), nitrate (for example SODIUMNITRATE), nitrosamine (for example N, N '-dinitrosopentamethylene tetramine), alkali metal borohydride (for example sodium borohydride).The more excellent compound of aerogenesis is nitrous acid and its nitre on the spot.Nitrous acid and its esters divide Jie's output bubble under acid pH value condition.Thiocarbamide can be used for quickening nitroso-group salt gas generating agent and decompose.Suitable hollow particle comprises little glass tiny balloon and resin material, for example P-F and urea formaldehyde.Suitable porous material comprises dilated mineral, for example perlite.
Usually in process of cooling, add gaseous fraction under envrionment temperature and pressure so that the latex that makes contains from the gas of about 0.05% to 50% volume.Usually the bubble diameter of occlusion is below 200 μ m, and it is better to be lower than 100 μ m, and better between 20 to 90 μ m, 40 to 70 μ m are especially good.Shared volume ratio is lower than 50%, and better, 30% to 10% is especially good between 40% and 30%.50% occluded gas exists better with the microspheres form of 20 to 90 μ m internal diameters, and internal diameter is that 40 to 70 μ m are better.
Can be according to emulsion explosive composition of the present invention by common emulsifying technology preparation.Like this, oxygen supply salt is higher than more than the salts solution ctystallizing point and can be soluble in the aqueous phase in temperature, and is more excellent in the time of 25 to 110 °.Modifying agent prepares respectively with the mixture (solution is more excellent) and the organic phase of the emulsifying agent of choosing wantonly, when the temperature identical, be prepared as better with salts solution, under stirring fast, water is being added to organic phase with the preparation emulsion explosive composition then, stir proceed to always form thing all till.Optional solid or gaseous fraction can under agitation add then, stir up to the latex that obtains homogeneous just to stop.
Can use according to emulsion explosive composition of the present invention like this, perhaps can be incorporated with the cartridge bag of suitable diameter.
Explain orally the present invention with reference to following Example, all the components or per-cent unless otherwise indicated all are basis representation with weight in these examples.
Example 1
This is a not foundation Comparative Examples of the present invention.
Under agitation heat ammonium nitrate (76.7 parts) and water (15.5 parts) to 85 ℃ to obtain the aqueous solution.Under stirring fast, the aqueous solution of heat is added to that (1.5 parts of sorbitan sesquialter oleates are in 3.8 parts of refined mineral oils) continue to stir up to obtaining uniform latex in the common emulsifier solution.
The specific conductivity that records gained latex sample by the said method in front in 60 ℃ the time is 150000 slight ohm/meter.
(2.5 parts of glass microspheres; C15/250 level Supplied by3M) is added in the latex residuum and thorough mixing therein.
With the mixture cooling, be packaged into then in the common cylinder paper cartridge bag of different diameter.The critical diameter of the mixture that discovery is made like this is 8mm.The cartridge bag of 25mm diameter stores down and tests periodically the capsular sensitivity with No. 8 detonators of standard in 10 ℃.
Can not detonate after storing for 9 weeks.
Example 2
Except that using following tensio-active agent, repeat the step of example 1.The mixture that uses 1 part of sorbitan sesquialter oleate and 0.5 part of modifying agent is as tensio-active agent.Modifying agent contains in two kinds of components of 70 ℃ of following stirring heating and makes 1 of polyisobutylene succinic anhydride (molecular-weight average 1200, molecular weight distribution reaches 3000) and thanomin: the polycondensate 1(mole).
The specific conductivity of latex is 48000 slight ohm/meter in the time of 60 ℃.According to example 1 said preparation, storage and test cartridge bag.Be no more than for 80 weeks storage time in the time of 10 ℃.
Example 3
Except that replacing thanomin to produce the step that repeats example 2 modifying agent with diethanolamine.The modifying agent that makes contains polyisobutylene succinic anhydride and diethanolamine 1: the polycondensate 1(mole).
The specific conductivity of latex is 50000 slight ohm/meter in the time of 60 ℃.
According to example 1 said preparation, storage and test cartridge bag, be no more than for 55 weeks storage time in the time of 10 ℃.
Example 4
Except that following difference, repeat the step of example 1.Save common tensio-active agent, be used as modifying agent as example 2 said 1.5 parts of polyisobutylene succinic anhydride/thanomin polycondensates.
The specific conductivity of 60 ℃ of following latexes is 250 slight ohm/meter.
Storage time is greater than 80 weeks when wrapping in 40 ℃ according to example 1 said preparation, storage and investigational agent.
Same cartridge bag stored down for 12 weeks at-30 ℃, and is still responsive to No. 8 detonators of standard after being warmed up to 5 ℃.On the contrary, the cartridge bag that use-case 1 said latex makes stores 1 day at-30 ℃ and then is warmed up to 5 ℃, and No. 8 detonator is failed its ignition.
Also pack into the common cylinder cartridge bag of a 38mm diameter of this latex sample.Can not be ignited by primacord fuse more than storing for 12 weeks under 40 ℃, this primacord fuse is attached to the cartridge bag outside, and every meter has 10 gram trinitrol (PENT) powder charges.The identical cartridge bag of use-case 8 mixtures preparation can not be ignited it after three weeks with said method caching in front and test.
Another part latex sample (2.5 kilograms) is packed in the common cylinder paper cartridge bag of a diameter 85mm, resists the turbulent performance that is caused by mechanical effect at ambient temperature by cartridge bag is fallen the concrete test from 30 feet (9.14m) height.The temperature that in cartridge bag, produced rise (intensification can owing to the crystallization of ammonium nitrate component) record by thermopair and be less than 3 ℃.The same cartridge bag of the mixture preparation of use-case 8 also stands fall down test, and the result heats up 12 ℃.
Example 5
Except that the modifying agent difference, repeat the step of example 4.1.5 parts of polyisobutylene succinic anhydride of modifying agent/thanomin polycondensate (1: 1) reacts with it with 1 mole of phosphoric acid and obtains the phosplate derivative.
The specific conductivity of this latex is 420 slight ohm/meter in the time of 60 ℃.
According to example 1 said preparation, storage and test cartridge bag, storage time is greater than 50 weeks in the time of 40 ℃.
Example 6
Except that the modifying agent difference, repeat example 4 steps.Modifying agent is 1.5 parts of polyisobutylene succinic anhydride (molecular-weight average 1200) and 2: 1 polycondensate of sorbyl alcohol.
The emulsion specific conductivity is 1900 slight ohm/meter in the time of 60 ℃.
By method preparation, storage and the test cartridge bag of example 1, storage time is greater than 40 weeks in the time of 40 ℃.
Example 7
Except that following difference, repeat the step of example 4.Oil phase is by 3.8 parts of Slackwax431(Interhaeiohalwaxes, and Agihcourt Ontario) forms and unique modifying agent is 1.5 parts of polyisobutylene succinic anhydride (molecular-weight average 1200)/thanomin (1: 1) polycondensate.Violent stirring forms latex, and contained droplet mean diameter is 1.5 μ m.
60 ℃ of following latex specific conductivity are 170 slight ohm/meter.
Then 2.5 parts of glass microspheres (C15/250) are added in the latex.
Wrap in 40 ℃ of following storage tives above 55 weeks by example 1 said preparation, storage and investigational agent.
Example 8
This is explanation Microcrystalline Wax and the mineral wax mixture Comparative Examples to the influence of specific conductivity, and they are well known as the tranquilizer of emulsion explosive in the prior art.
Use-case 1 method is by the latex of following component preparation.
Part
Ammonium nitrate 64.85
Refined mineral oil 1.1
Paraffin (fusing point 50-62 ℃) 1.65
Microcrystalline Wax (72 ℃ of fusing points) 1.65
Sorbitan sesquialter oleate 1.75
Water 11.5
SODIUMNITRATE 15.0
Microballoon (C15/250) 2.5
The specific conductivity of 60 ℃ of following latexes is 100000 slight ohm/meter.
According to example 1 said preparation, store and the test cartridge bag 40 ℃ of following storage time in about 10 weeks.
This latex sample is also packed in the common cylinder cartridge bag of diameter 38mm, in 40 ℃ store down 3 week the back cartridge bags can not ignite by primacord fuse, primacord fuse is attached to the cartridge bag outside, every meter has 10 gram trinitrol (PENT) powder charges.Make the mixture of use-case 4 prepare same cartridge bag, store and test, after surpassing for 12 weeks, still can be detonated with the said test method in front.
Pack into the common cylinder paper cartridge bag of 85mm diameter of another part latex sample (2.5 kilograms).By being fallen the concrete test from 30 meters (9.14 meters) height, cartridge bag resists the turbulent performance that causes by mechanical effect at ambient temperature.The temperature that produces in the cartridge bag raise (intensification can owing to the crystallization of ammonium nitrate component) be measured as 12 ℃ with thermopair.
Example 9
Except that using following different surfaces promoting agent, repeat the step of example 1.600) and the mixture of 1: 1 mole of polycondensate of sorbyl alcohol the tensio-active agent that uses is sorbitan sesquialter oleate (0.75 part) and poly--12-oxystearic acid (molecular weight:.
The specific conductivity of this latex is 50000 slight ohm/meter under 60 ℃.
According to example 1 said preparation, store and the test cartridge bag, storage time is greater than 20 weeks in the time of 10 ℃.
Example 10
Make emulsion by example 1 said method by following component: ammonium nitrate (65.5 parts), SODIUMNITRATE (15.0 parts), water (11.0 parts), paraffin (4.5 parts), 1500) and 1: 1 mole the polycondensate of three (methylol) amine-methane dehydrated sorbitol mono-fatty acid ester (0.75 part) and poly--12-oxystearic acid (molecular weight:.
The specific conductivity of 60 ℃ of following latexes is 50000 slight ohm/meter.
Then with (2.5 parts: the C15/250 type) be added in the latex and go of glass microspheres.
According to example 1 said preparation, storage and test cartridge bag, 10 ℃ of following cartridge bag storage tives are greater than 25 weeks.
Example 11
Except that the modifying agent difference, repeat the step of example 4.Modifying agent is 1.5 parts of polyisobutylene succinic anhydride (molecular-weight average 1200) and ethylene glycol 1: the 1(mol ratio) polycondensate.
The specific conductivity of 60 ℃ of following latexes is 320 slight ohm/meter.
According to example 1 said preparation, store and the test cartridge bag, storage time is greater than 30 weeks in the time of 40 ℃.
Example 12
Repeat example 4 steps except that the modifying agent difference, modifying agent is 1.5 parts of polyisobutylene succinic anhydride (molecular-weight average 1200) and dimethyl amine propyl ammonium 1: the 1(mol ratio) polycondensate.
60 ℃ of following latex specific conductivity are 650 slight ohm/meter.
According to example 1 said preparation, store and the test cartridge bag, 40 ℃ of following storage tives are greater than 30 weeks.
Example 13
Except that the modifying agent difference, repeat the step of example 4.Modifying agent is 1 of 1.5 parts of poly-isobutyl-succinyl oxides (molecular-weight average 1200) and a diethyl amido propyl ammonium: the 1(mol ratio) polycondensate.
The specific conductivity of 60 ℃ of following latexes is 390 slight ohm/meter.
According to example 1 said preparation, store and the test cartridge bag, 40 ℃ of following storage tives are greater than 25 weeks.
Example 14
Except that the modifying agent difference, repeat the step of example 4.Modifying agent is 1.5 parts of polyisobutylene succinic anhydride (molecular-weight average 1200) and N, 1: 1 polycondensate of N-N-dimethyl amine alcoholic acid.
Specific conductivity in 60 ℃ of following latexes is 550 slight ohm/meter.
According to example 1 said preparation, store and the test cartridge bag, 40 ℃ of following storage tives are greater than 25 weeks.
Example 15
Except that the modifying agent difference, repeat the step of example 4.Modifying agent is 1.5 parts of polyisobutylene succinic anhydride (molecular-weight average 1200) and 1: 1 polycondensate of Sorbitol Powder.
The specific conductivity of 60 ℃ of following latexes is 650 slight ohm/meter.
By example 1 said preparation, storage and test cartridge bag, in 40 ℃ of following storage tives greater than 25 weeks.
Example 16
Except that the modifying agent difference, repeat the step of example 4.Modifying agent is 1.5 parts of polyisobutylene succinic anhydride (molecular-weight average 1200) and glycine 1: the 1(mol ratio) polycondensate.
The specific conductivity of 60 ℃ of following latexes is 230 slight ohm/meter.
According to example 1 said preparation, store and the test cartridge bag, 40 ℃ of following storage tives are greater than 37 weeks.
Example 17
Except that the modifying agent difference, repeat the step of example 4.Modifying agent is 1 of 1.5 parts of polyisobutylene succinic anhydride (molecular-weight average 800) and a thanomin: the 1(mol ratio) polycondensate.
The specific conductivity of 60 ℃ of following latexes is 440 slight ohm/meter.
According to example 1 said preparation, store and the test cartridge bag, 40 ℃ of following storage tives are greater than 20 weeks.
Example 18
Except that the modifying agent difference, repeat the step of example 4.Modifying agent is 1.5 parts of polyisobutene allyl succinic anhydrides (molecular-weight average 1200) thanomin and Monochloro Acetic Acid 1: 1: the polycondensate 1(mol ratio).
The specific conductivity of 60 ℃ of following latexes is 420 slight ohm/meter.
According to example 1 said preparation, store and the test cartridge bag, under 40 ℃, storage time is greater than 30 weeks.
Example 19
Prepare basic latex according to example 1 step by following component.
Part
Ammonium nitrate 78.7
Water 16.0
Slackwax, 431(purchases InternationalWaxes) 3.0
Refined mineral oil 0.8
Tensio-active agent
*1.5
Tensio-active agent
*1: 1 mole of polycondensate for polyisobutylene succinic anhydride (molecular-weight average 1200) and thanomin.
Basic latex specific conductivity is 180 slight ohm/meter under 60 ℃.
2.5 part glass microsphere (C15/250; Supply with by 3M) and 87.5 parts of basic latexes of 10 parts of porous ammonium nitrate beads addings in.
(seeing example 20) do not consider solid ammonium nitrate impurity (it causes that usually explosive sensitivity sharply descends) under the situation that prior art surfactants exists.
Mixture powder charge in 25mm diameter paper detonator is in 40 ℃, stores at least 55 weeks, to being responsive with No. 8 blasting cap initiations of standard.
Example 20
This is not according to Comparative Examples of the present invention.
What use except that tensio-active agent is the sorbitan sesquialter oleate, repeats the step of example 19.
The specific conductivity of basic latex is 170000 slight ohm/meter under 60 ℃.
According to example 19 said preparations, storage and test cartridge bag, after 40 ℃ of following 1 weeks of storage, can not detonate
Example 21
Mix 60 parts of example 4 said latexes and 40 parts of ammonium nitrate/oil fuel (ANFO) (94 parts of ammonium nitrate bead/6 part oil fuel) and make pyrotechnic composition.
Mixture is loaded in the wet borehole of a 15Cm diameter, and one week of filling back is with 400 milligrams of Peng Tuolite (50: 50, too peace/tritonal) cap sensitive.
The said latex that contains sorbitan sesquialter oleate prepares similar explosive in the use-case 1, loads back 1 day, can not detonate.
Example 22
Except that the modifying agent difference, repeat the step of example 4.Modifying agent is 1 of 1.5 parts of polyisobutylene succinic anhydride (molecular-weight average 1200, wherein polyisobutenyl contains 85% iso-butylene, 10%2-butylene and 5%1-butylene) and a thanomin: the 1(mol ratio) polycondensate.
The specific conductivity of 60 ℃ of following latexes is 320 slight ohm/meter.
According to example 1 said preparation, store and the test cartridge bag, 40 ℃ of following storage tives are greater than 25 weeks.
Example 23
Except that the modifying agent difference, repeat the step of example 4.Modifying agent is kept to 1.5 parts of polyisobutylene succinic anhydride (molecular-weight average 1200) and benzoglyoxaline 1: the 1(mol ratio) polycondensate.
60 ℃ of following emulsion specific conductivity 720 slight ohm/meter.
According to example 1 said preparation, store and the test cartridge bag, 40 ℃ of following storage tives are greater than 26 weeks.
Example 24
This example explanation original place forms modifying agent.
1.42 a part polyisobutylene succinic anhydride (molecular-weight average 1200) under agitation slowly is added in 0.08 part of thanomin.Added back 5 minutes, and added 3.8 parts of refined mineral oils, mixture was heated 4 hours in 70-80 ℃.By adding the solution of 78.7 parts of ammonium nitrate in 16 parts of water in said mixture and be heated to 80 ℃ method, directly form emulsion explosive.
The latex of Xing Chenging specific conductivity in the time of 60 ℃ is 300 slight ohm/meter like this.Add glass microsphere (2.5 parts of C15/250 level Supplied by 3M) as storage and test latex as described in the example 1,40 ℃ of following storage tives are greater than 55 weeks.
Example 25
Except that the modifying agent difference, repeat the step of example 4.Modifying agent is a mixture, contain (a) a polyisobutylene succinic anhydride (molecular-weight average 1200) and thanomin 1: the 1(mol ratio) polycondensate and (b) polycondensate of 0.5 part of end carboxyl polyethylene (molecular-weight average 2000) (in the presence of catalyzer in 120-150 ℃ by the atmospheric oxidation polyethene preparation) and 1: 1 mol ratio of three (methylol) aminomethane.
60 ℃ of following latex specific conductivity are 95 slight ohm/meter.
According to example 1 said preparation, store and the test cartridge bag, 40 ℃ of following storage tives are greater than 20 weeks.
Example 26
Except that following difference, repeat the step of example 25.Oxidic polyethylene and excessive three (methylol) amido methane reaction obtain a kind of about 1: oxidic polyethylene three (methylol) the amido methane addition compound 2(mol ratio).0.5 part such addition compound and 1 part 1: the 1(mol ratio) polyisobutylene succinic anhydride/thanomin polycondensate uses jointly.
The specific conductivity of 60 ℃ of following latexes is 980 slight ohm/meter.
As preparation as described in the example 1, store and the test cartridge bag, 40 ℃ of following storage tives are greater than 20 weeks.
Example 27
Except that the modifying agent difference, repeat the step of example 4.Modifying agent is a mixture, contain 1: 1 mole of condensation product of (a) 1 part of polyisobutylene succinic anhydride (molecular-weight average 1200) and dimethanolamine and (b) 0.5 part have the hydrogenation polyisoamylene (molecular-weight average 1000) of holding carboxyl and 1: 1 mole polycondensate of Sorbitol Powder.
The specific conductivity of 60 ℃ of following latexes is 490 slight ohm/meter.
As preparation as described in the example 1, store and the test cartridge bag, be not more than for 25 weeks 40 ℃ of following storage tives.
Example 28
Except that the modifying agent difference, repeat the step of example 4.Modifying agent is a kind of mixture, and it consists of 1: 1 mole the condensation product of (a) 1 part of polyisobutylene succinic anhydride (molecular-weight average 1200) and Sorbitol Powder and (b) polycondensate of 0.5 part of its chlorinated polypropylene (molecular-weight average 1500) (an end carboxylic acid group is arranged) and three (methylol) amido methane.
The specific conductivity of 60 ℃ of following latexes is 790 slight ohm/meter.
As preparation as described in the example 1, storage and test cartridge bag, 40 ℃ of following storage tives are greater than 20 weeks.
Claims (25)
1, a kind of emulsion explosive composition that contains discontinuous phase that oxygen-supplying component is arranged and form the organic medium of external phase is characterized in that, oxygen-supplying component and organic medium can form latex, when not having the auxiliary that replenishes, be no more than 60000 slight ohm/meter in 60 ℃ of specific conductivity that record this latex.
2, the mixture according to claim 1 is characterized in that, this mixture contains a kind of specific conductivity modifying agent.
3, the mixture according to claim 2 is characterized in that, modifying agent contains oleophilic moiety and hydrophilic segment.
4, the mixture according to claim 3 is characterized in that, oleophilic moiety contains the chain structure of skeleton sequence that contains 10 at least but be no more than the atom of 500 connections.
5, the mixture according to claim 4 is characterized in that, chain structure contains a monoolefine polymer, and its monomer contains 2 to 6 carbon atoms.
6, it is characterized in that oleophilic moiety contains poly-(alkane (alkene) base) succinyl oxide according to each mixture in the claim 3 to 5.
7, the mixture according to claim 6 is characterized in that, oleophilic moiety contains poly-(iso-butylene) succinyl oxide.
8, the mixture according to claim 3 is characterized in that, oleophilic moiety contains from least one saturated or unsaturated long-chain polymkeric substance that (reaching 25 carbon atoms)-hydroxyl-first carboxylic acid lactoneization obtains.
9, the mixture according to claim 8 is characterized in that, oleophilic moiety contains poly-(12-hydroxyl-stearic acid).
10, each the mixture according to claim 3 to 9 is characterized in that hydrophilic segment contains a part amount and is no more than 450 polarity organic radical.
11, each the mixture according to claim 3 to 10 is characterized in that hydrophilic segment is monomeric or oligomerisation.
12, the mixture according to claim 11 is characterized in that, the monomer hydrophilic segment is that its intramolecular anhydride, amine, acid amides, alkanolamine or heterocyclic derivatives get from more than one alcohol.
13, the mixture according to claim 11 is characterized in that, the oligomerisation hydrophilic segment contains poly-(oxygen ethene) base of no more than 10 ethylene oxide units.
14, it is characterized in that according to each the mixture in claim 2 to 7 and 10 to 12 modifying agent contains polyisobutenyl succinic anhydride and thanomin polycondensate.
15, each the mixture according to the front claim is characterized in that it contains latex, does not have the auxiliary of replenishing, and is no more than 2000 slight ohm/meter in 60 ℃ of specific conductivity that record this latex.
16, a kind of method for preparing emulsion explosive composition, comprise emulsification oxygen-supplying component and organic medium to form latex, oxygen-supplying component forms the part discontinuous phase at least in latex, and organic medium forms the partial continuous phase at least, it is characterized in that, emulsifying effect is finished in the presence of modifying agent, and it can lower the specific conductivity of the latex that is formed by oxygen-supplying component and organic medium, records its value and be no more than 60000 slight ohm/meter when replenishing under the auxiliary situation in 60 ℃.
17, the method according to claim 16 is characterized in that modifying agent contains oleophilic moiety and hydrophilic segment.
18, any method according to claim 16 or 17 is characterized in that, oleophilic moiety contains and contains 10 chain structures that are no more than the skeleton sequence of 500 connection carbon atoms at least.
19, the arbitrary method according to claim 16 to 18 is characterized in that, oleophilic moiety contains poly-(alkane (alkene) base) succinyl oxide.
20, the method according to claim 19 is characterized in that oleophilic moiety contains poly-(iso-butylene) succinyl oxide.
21, the method according to claim 17 is characterized in that, oleophilic moiety contains at least one saturated or unsaturated long-chain polymkeric substance that (reaching 25 carbon atoms)-hydroxyl-first carboxylic acid lactoneization obtains.
22, the method according to claim 21 is characterized in that, oleophilic moiety contains poly-(12-hydroxyl-stearic acid).
23, the arbitrary method according to claim 17 to 22 is characterized in that, hydrophilic segment contains a molecular weight and is no more than 450 polarity organic radical.
24, the arbitrary method according to claim 17 to 23 is characterized in that modifying agent contains the polycondensate of polyisobutenyl succinic anhydride and thanomin.
25, explosive loading is characterized in that, powder charge contains arbitrary emulsion explosive composition of with good grounds claim 1 to 5 or the emulsion explosive composition that makes according to claim 16 to 24 either party's methods.
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN85101581.6A CN1004625B (en) | 1985-04-01 | 1985-04-01 | Emulsion explosive composition |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN85101581.6A CN1004625B (en) | 1985-04-01 | 1985-04-01 | Emulsion explosive composition |
Publications (2)
| Publication Number | Publication Date |
|---|---|
| CN85101581A true CN85101581A (en) | 1986-10-29 |
| CN1004625B CN1004625B (en) | 1989-06-28 |
Family
ID=4791917
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| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| CN85101581.6A Expired CN1004625B (en) | 1985-04-01 | 1985-04-01 | Emulsion explosive composition |
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| Country | Link |
|---|---|
| CN (1) | CN1004625B (en) |
Cited By (3)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN103755503A (en) * | 2014-01-23 | 2014-04-30 | 葛洲坝易普力股份有限公司 | Polymer emulsifier for mixed emulsified explosive and preparation method of polymer emulsifier |
| CN113563141A (en) * | 2020-04-29 | 2021-10-29 | 南京理工大学 | Industrial detonating cord drug core prepared from energetic material byproducts |
| CN115650809A (en) * | 2022-09-28 | 2023-01-31 | 安徽理工大学 | Colloidal ammonium amine explosive and preparation method thereof |
Families Citing this family (1)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| US7771550B2 (en) * | 2005-10-07 | 2010-08-10 | Dyno Nobel, Inc. | Method and system for manufacture and delivery of an emulsion explosive |
-
1985
- 1985-04-01 CN CN85101581.6A patent/CN1004625B/en not_active Expired
Cited By (5)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN103755503A (en) * | 2014-01-23 | 2014-04-30 | 葛洲坝易普力股份有限公司 | Polymer emulsifier for mixed emulsified explosive and preparation method of polymer emulsifier |
| CN103755503B (en) * | 2014-01-23 | 2016-03-30 | 葛洲坝易普力股份有限公司 | A kind of the mixed loading emulsion explosive macromolecule emulsifier and preparation method thereof |
| CN113563141A (en) * | 2020-04-29 | 2021-10-29 | 南京理工大学 | Industrial detonating cord drug core prepared from energetic material byproducts |
| CN115650809A (en) * | 2022-09-28 | 2023-01-31 | 安徽理工大学 | Colloidal ammonium amine explosive and preparation method thereof |
| CN115650809B (en) * | 2022-09-28 | 2023-10-10 | 安徽理工大学 | Colloidal ammonium amine explosive and preparation method thereof |
Also Published As
| Publication number | Publication date |
|---|---|
| CN1004625B (en) | 1989-06-28 |
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