CN101357873A - Continuous technique for preparing emulsifying explosive and charging - Google Patents
Continuous technique for preparing emulsifying explosive and charging Download PDFInfo
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- CN101357873A CN101357873A CNA2007100753913A CN200710075391A CN101357873A CN 101357873 A CN101357873 A CN 101357873A CN A2007100753913 A CNA2007100753913 A CN A2007100753913A CN 200710075391 A CN200710075391 A CN 200710075391A CN 101357873 A CN101357873 A CN 101357873A
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- powder charge
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- phase solution
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- 239000002360 explosive Substances 0.000 title claims abstract description 23
- 238000000034 method Methods 0.000 title abstract description 9
- 230000001804 emulsifying effect Effects 0.000 title description 3
- 239000012071 phase Substances 0.000 claims abstract description 40
- 239000004816 latex Substances 0.000 claims abstract description 34
- 229920000126 latex Polymers 0.000 claims abstract description 34
- 238000001816 cooling Methods 0.000 claims abstract description 27
- 210000003022 colostrum Anatomy 0.000 claims abstract description 26
- 235000021277 colostrum Nutrition 0.000 claims abstract description 26
- 239000000839 emulsion Substances 0.000 claims abstract description 19
- 239000008346 aqueous phase Substances 0.000 claims abstract description 18
- 238000004806 packaging method and process Methods 0.000 claims abstract description 13
- 230000003068 static effect Effects 0.000 claims abstract description 11
- 238000002156 mixing Methods 0.000 claims abstract description 8
- 239000000843 powder Substances 0.000 claims description 60
- 206010070834 Sensitisation Diseases 0.000 claims description 50
- 230000008313 sensitization Effects 0.000 claims description 50
- 239000003921 oil Substances 0.000 claims description 25
- 238000005516 engineering process Methods 0.000 claims description 23
- 238000010924 continuous production Methods 0.000 claims description 21
- XLYOFNOQVPJJNP-UHFFFAOYSA-N water Substances O XLYOFNOQVPJJNP-UHFFFAOYSA-N 0.000 claims description 17
- 239000000126 substance Substances 0.000 claims description 13
- 239000003995 emulsifying agent Substances 0.000 claims description 9
- 239000011521 glass Substances 0.000 claims description 8
- 239000002480 mineral oil Substances 0.000 claims description 8
- 235000010446 mineral oil Nutrition 0.000 claims description 8
- 239000011159 matrix material Substances 0.000 claims description 7
- 239000010451 perlite Substances 0.000 claims description 7
- 235000019362 perlite Nutrition 0.000 claims description 7
- 210000000481 breast Anatomy 0.000 claims description 6
- 150000001875 compounds Chemical class 0.000 claims description 6
- 239000002985 plastic film Substances 0.000 claims description 5
- 229920006255 plastic film Polymers 0.000 claims description 5
- PAWQVTBBRAZDMG-UHFFFAOYSA-N 2-(3-bromo-2-fluorophenyl)acetic acid Chemical compound OC(=O)CC1=CC=CC(Br)=C1F PAWQVTBBRAZDMG-UHFFFAOYSA-N 0.000 claims description 4
- 238000009837 dry grinding Methods 0.000 claims description 3
- 239000012530 fluid Substances 0.000 claims description 3
- 238000007670 refining Methods 0.000 abstract 1
- 238000010792 warming Methods 0.000 abstract 1
- 239000003795 chemical substances by application Substances 0.000 description 14
- 238000002360 preparation method Methods 0.000 description 9
- 238000004519 manufacturing process Methods 0.000 description 7
- 239000002253 acid Substances 0.000 description 6
- 239000000203 mixture Substances 0.000 description 5
- 238000004945 emulsification Methods 0.000 description 4
- 230000001235 sensitizing effect Effects 0.000 description 4
- 238000003756 stirring Methods 0.000 description 4
- 238000004880 explosion Methods 0.000 description 3
- 238000007654 immersion Methods 0.000 description 3
- 230000015556 catabolic process Effects 0.000 description 2
- 239000000084 colloidal system Substances 0.000 description 2
- 238000001035 drying Methods 0.000 description 2
- 238000011068 loading method Methods 0.000 description 2
- 239000000463 material Substances 0.000 description 2
- 238000007789 sealing Methods 0.000 description 2
- 235000013599 spices Nutrition 0.000 description 2
- 238000003860 storage Methods 0.000 description 2
- JLPULHDHAOZNQI-ZTIMHPMXSA-N 1-hexadecanoyl-2-(9Z,12Z-octadecadienoyl)-sn-glycero-3-phosphocholine Chemical compound CCCCCCCCCCCCCCCC(=O)OC[C@H](COP([O-])(=O)OCC[N+](C)(C)C)OC(=O)CCCCCCC\C=C/C\C=C/CCCCC JLPULHDHAOZNQI-ZTIMHPMXSA-N 0.000 description 1
- 229920013649 Paracril Polymers 0.000 description 1
- 229910000831 Steel Inorganic materials 0.000 description 1
- 230000009286 beneficial effect Effects 0.000 description 1
- 239000002131 composite material Substances 0.000 description 1
- 239000002826 coolant Substances 0.000 description 1
- 239000003814 drug Substances 0.000 description 1
- 238000013467 fragmentation Methods 0.000 description 1
- 238000006062 fragmentation reaction Methods 0.000 description 1
- 238000009413 insulation Methods 0.000 description 1
- 239000007788 liquid Substances 0.000 description 1
- 238000012986 modification Methods 0.000 description 1
- 230000004048 modification Effects 0.000 description 1
- 239000012188 paraffin wax Substances 0.000 description 1
- 238000003672 processing method Methods 0.000 description 1
- 238000005086 pumping Methods 0.000 description 1
- 238000012797 qualification Methods 0.000 description 1
- 230000035945 sensitivity Effects 0.000 description 1
- 238000010008 shearing Methods 0.000 description 1
- 238000010129 solution processing Methods 0.000 description 1
- 229940083466 soybean lecithin Drugs 0.000 description 1
- 229910001220 stainless steel Inorganic materials 0.000 description 1
- 239000010935 stainless steel Substances 0.000 description 1
- 239000010959 steel Substances 0.000 description 1
- 239000001993 wax Substances 0.000 description 1
- 238000005303 weighing Methods 0.000 description 1
- 230000003245 working effect Effects 0.000 description 1
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Abstract
The invention provides a continuous producing process for pharmacy and charging of emulsion explosive, which comprises the following steps: (1) aqueous phase solution and oil phase solution are respectively prepared; (2) the aqueous phase solution and the oil phase solution are delivered into a colostrum device for mixing, and after the process of colostrum, the aqueous phase solution and the oil phase solution are delivered into a static mixer for refining colostrum; (3) after the refined colostrum latex are delivered into a sensitized charging system for sensitized treatment, charging is carried out and after being cooled by a cooling system, the products are delivered to a packaging system for packaging. The technique proposal of the process is characterized by no warming after the process of the colostrum, high safety, and little damage of latex.
Description
Technical field
The invention belongs to emulsion explosive production technology, relate in particular to a kind of emulsion explosive pharmacy and powder charge continuous production technology.
Background technology
At present, there are a lot of problems in emulsion explosive continuous production technology in the prior art.
At first, in the existing emulsion explosive continuous production technology, generally comprise preparation aqueous phase solution and oil-phase solution, colostrum, smart breast, cooling, sensitization powder charge and packaging and other steps successively.Adopt such processing method, latex is made the back and is cooled off colloid by continuous enclosed cooler, steel band cooler or immersion continuous cooling equipment earlier, after the colloid temperature is cooled to 40～70 ℃ of scopes from 100 ℃ ± 15 ℃, add chemical sensitizer or physical sensitization agent again, form the emulsion explosive of chemical sensitization or physical sensitization.Adopt the technology of this back sensitization powder charge of cooling earlier, during the latex cooling,, all can produce in various degree damage latex because of it directly soaks or is subjected to cooler to stir, scrape.
Secondly, in the existing emulsion explosive continuous production technology, smart newborn device all uses the emulsor of dynamic shearing formula, and the power of consumption is very big and production capacity is little.And, adopting rotary smart emulsor, the latex temperature generally is higher than water, oil phase temperature after the emulsification, no matter have or not sealing, in oil, water cutout back or the cutout of sealing water coolant, still in the running as emulsor, all easily produce heat built-up and explosion caused danger, thereby security is relatively poor.
At last, because of medicine attitude thickness that becomes after cooling, increased the difficulty of follow-up powder charge, sensitization powder charge system generally adopts the paper web charge machine to carry out powder charge, and loading rate is low.
Summary of the invention
The technical problem that the embodiment of the invention will solve does not have intensification after being to provide a kind of emulsification, and is safe, and the latex damage is few, emulsion explosive pharmacy and powder charge continuous production technology.
The embodiment of the invention is achieved in that a kind of emulsion explosive pharmacy and powder charge continuous production technology, comprises the steps:
(1) prepares aqueous phase solution and oil-phase solution respectively;
(2) press processing compound, aqueous phase solution and oil-phase solution are conveyed into the mixing of colostrum device respectively, carry out colostrum, send into static mixer then and carry out the essence breast;
(3) the essence latex is sent into sensitization powder charge system and carried out sensitization processing back powder charge, after the cooling system cooling, deliver to packaging system again and pack.
Compared with prior art, the technical scheme that the embodiment of the invention provides, because smart newborn device does not adopt rotary smart emulsor, and adopt static mixer, thereby avoided because of latex temperature after the emulsification is higher than water, the oil phase temperature produces the explosion caused danger of heat built-up.And the embodiment of the invention adopts the technology of first sensitization powder charge postcooling, the direct immersion when having avoided the latex cooling, or be subjected to cooler stirring, scrape, thereby also avoided the damage in various degree that thus latex is produced.
Description of drawings
Accompanying drawing is in the embodiment of the invention emulsion explosive pharmacy and powder charge continuous production technology that provide, the structural representation of device systems one preferred embodiment of being adopted.
Embodiment
In order to make the technical problem to be solved in the present invention, technical scheme and beneficial effect clearer,, the present invention is further elaborated below in conjunction with drawings and Examples.Should be appreciated that specific embodiment described herein only in order to explanation the present invention, and be not used in qualification the present invention.
Emulsion explosive pharmacy and powder charge continuous production technology that the embodiment of the invention provides comprise the steps:
(1) prepares aqueous phase solution and oil-phase solution respectively;
(2) press processing compound, aqueous phase solution and oil-phase solution are conveyed into the mixing of colostrum device respectively, carry out colostrum, send into static mixer then and carry out the essence breast;
(3) the essence latex is sent into sensitization powder charge system and carried out sensitization processing back powder charge, after the cooling system cooling, deliver to packaging system again and pack.
In the embodiment of the invention, sensitization powder charge system is physical sensitization powder charge system, chemical sensitization powder charge system or physics, chemically composited sensitization powder charge system.Wherein physical sensitization powder charge system comprises perlite system or glass microballon system.The physical sensitization powder charge system of smart latex through comprising described glass microballon system carries out sensitization and handles powder charge again, can directly deliver to packaging system and pack without described cooling system.In the embodiment of the invention, oil phase and aqueous phase solution processing compound are the 3-6% that oil-phase solution accounts for two total solution weight, and aqueous phase solution accounts for the 94-97% of gross weight.Aqueous phase solution is the ammonium nitrate solution of 87-92% concentration; Oil-phase solution is made up of mineral oil and emulsifying agent, and mineral oil and emulsifying agent are mineral oil well known in the art and emulsifying agent, and for example emulsifying agent can be selected SPAM80 and/or soybean lecithin for use.Its mineral oil in fluid accounts for the 66.6%-91.6% of oil phase weight, and emulsifying agent accounts for the 8.4%-33.3% of oil phase weight.In this oil phase material, do not add the paraffin and the compound wax of easily solidifying, pipeline and heat-insulation system are simplified, delivery safety is better.
In the embodiment of the invention, colostrum adopts the matrix spiral pump to carry, and this matrix spiral pump is provided with cutout dry grinding, overtemperature, superpressure safeguard protection deadman control, and rotating speed is lower than 200 rev/mins.The rotor of spiral pump adopts stainless steel 90, and stator adopts the paracril manufacturing, and spiral pump increases work-ing life greatly under this technical recipe.About 8 kilotons are just changed stator one time, have changed once life-span height 8 times than about 1 kiloton of the screw pump stator of present use.
In the embodiment of the invention, the colostrum device is a small volume, is no more than 120L colostrum device.This colostrum body is long-pending small and exquisite, rotating speed is low (300～600 rev/mins) and power little (3 kilowatts), has improved security.
In the embodiment of the invention, charge machine adopts the plastic film charge machine, preferred big production capacity plastic film charge machine.
In the embodiment of the invention, latex is carried under 88～92 ℃.Under this temperature, add sensitizing agent after because good fluidity, easily carry and mix, difficult generation is solidified plugging, breakdown of emulsion and is produced highly compressed danger.
Embodiment
Adopt device systems shown in the drawings in the embodiment of the invention.According to technical process, this device systems order of connection is followed successively by oil phase, water preparation system, emulsifying system, sensitization powder charge system, cooling system and packaging system 19.
In oil phase, the water preparation system, the water preparation system comprises crusher 1, worm conveyor 2, molten jar 3 of water, toothed gear pump 4, water basin 5 and water pump 6; The oil phase preparation system comprises molten jar 33 of oil phase, toothed gear pump 32, oil phase storage tank 31 and oil phase pump 30.
Emulsifying system comprises colostrum device 7, matrix spiral pump 8 and static mixer 9.
Sensitization powder charge system comprises chemical sensitization powder charge system and physics, chemically composited sensitization powder charge system.Wherein, chemical sensitization powder charge system comprises latex pump 10, whipping agent transferpump 11, whipping agent jar 12, back acid jar 13, the sour transferpump 14 in back, mixing tank 15 and charge machine 16; Physics, chemically composited sensitization powder charge system comprise charge machine 20, dynamic mixer 21, the sour transferpump 22 in back, back acid jars 23, whipping agent transferpump 24, whipping agent jar 25, latex pump 26, latex pump 27, kneader 28 and perlite or glass microballon system 29.
Cooling system comprises that powder stick cooling system 17 and powder stick dry up system 18.
The colostrum device is a small volume in the system, is no more than 120L colostrum device; Matrix spiral pump 8 is provided with cutout dry grinding, overtemperature, superpressure safeguard protection deadman control, and rotating speed is lower than 200 rev/mins.Charge machine is big production capacity plastic film charge machine in the sensitization powder charge system.
Emulsion explosive pharmacy that present embodiment provides and powder charge serialization device systems, according to arts demand wherein sensitization powder charge system physics, chemically composited sensitization powder charge system or chemical sensitization powder charge system can only be set separately.In addition, sensitization powder charge system also can only be provided with the physical sensitization powder charge system that comprises latex pump 26 and latex pump 27, kneader 28, perlite or glass microballon system 29 and charge machine 20 separately.And when being the glass microballon system in this physical sensitization powder charge system, can need not complicated cooling system this moment.
Adopt above device systems, with reference to the accompanying drawings, emulsion explosive pharmacy and powder charge continuous production process that present embodiment provides are as follows:
1, preparation aqueous phase solution and oil-phase solution.
Add the water entry and mix jars 3, after steam air pressure should not surpass under the condition of 0.25Mpa, be heated to 95 ℃, with industrial ammonium nitrate through crusher 1 fragmentation, through spiral conveyer 2, send into water jar 3, when solution temperature is raised to 75 when spending, stirs and continue to be heated to 88～90 ℃ of technological temperatures, being mixed with concentration is 87-92% supersaturation ammonium nitrate liquid, flow into toothed gear pump 4 through pipeline, send into water basin 5, be incubated standby;
Take by weighing oil phase material mineral oil and emulsifying agent and add oil phase molten jar 33, be heated to 60～70 ℃ of technological temperatures, dissolve, be incubated standby after toothed gear pump 32 pumps into oil phase storage tank 31.Its mineral oil in fluid accounts for the 66.6%-91.6% of oil phase weight, and emulsifying agent accounts for the 8.4%-33.3% of oil phase weight.
2, the gross weight with water, oil phase two solution is a benchmark, get the aqueous phase solution that accounts for gross weight 94% and 6% oil-phase solution, aqueous phase solution is through water pump 6, and oil-phase solution is sent into colostrum device 7 respectively through oil phase pump 30 and carried out colostrum, sends into static mixer then and carries out the essence breast; Colostrum is sent into static mixer 9 through matrix through spiral pump 8, forms smart latex.
3, select physical sensitization, chemical sensitization or physics, chemically composited sensitization as required, and the corresponding subsequent step of taking.
(1) preparation physics sensitizing explosive.
The latex that static mixer 9 comes out is sent in the perlite system 29, mixing in kneader 28, send into charge machine 20 by latex pump 26 and latex pump 27, after sending in the powder stick cooling system 17 cooling again, enter powder stick and dry up drying in the system 18, enter at last in the automatic packaging system 19 and pack.As changing the perlite system into the glass microballon system, can directly deliver to automatic packaging system 19 and pack without cooling system.
(2) preparation chemical sensitization explosive.
During chemical sensitization, smart latex is sent into dynamic mixer 15 through latex pump 10, chemical sensitizer is by whipping agent transferpump 11 simultaneously, whipping agent in the whipping agent jar 12 is sent in the dynamic mixer 15, the sour transferpump in back 14 will back acid back acid in jars 13 also send into mix in the dynamic mixer 15 after, form spice, enter charge machine 16 simultaneously, be packaged into required explosive cartridge, after sending in the powder stick cooling system 17 cooling again, enter powder stick and dry up drying in the system 18, enter at last in the automatic packaging system 19 and pack.
(3) preparation composite sensitization explosive.
Carrying out physics, during chemically composited sensitization, the latex that static mixer 9 comes out enters in the perlite system 29, sneak into the physics sensitizing agent, mixing in kneader 28, send in the dynamic mixer 21 by latex pump 26 and latex pump 27, chemical sensitizer is by whipping agent transferpump 24 simultaneously, whipping agent in the whipping agent jar 25 is sent in the dynamic mixer 21, the sour transferpump in back 22 will back acid back acid in jars 23 also send into mix in the dynamic mixer 21 after, after being mixed into spice, enter charge machine 20 again, be packaged into explosive cartridge, successively through powder stick cooling system 17, powder stick dries up and enters automatic packaging system 19 after the system 18 and pack.
The technical scheme that adopts the embodiment of the invention to provide owing to adopt static mixer, thereby has avoided that the latex temperature is higher than water after the emulsification, the oil phase temperature produces heat built-up and explosion caused danger.Owing to adopt emulsion explosive pharmacy and the powder charge continuous process method of first sensitization powder charge postcooling, the direct immersion when having avoided the latex cooling, or be subjected to cooler stirring, scrape, thereby also avoided thus damage in various degree to the latex generation.The colostrum device is volume small and exquisite pre-breast jar, rotating speed low (300～600 rev/mins), power little (3 kilowatts), makes security better; Emulsoid is to carry under higher temperature (88～92 degree), add sensitizing agent after because good fluidity, easily carry and mix, difficult generation is solidified plugging, breakdown of emulsion and is produced highly compressed danger.Chemical sensitizer is to add enter charge machine after pumping before, has the emulsified detonator loading of sensitivity smooth and easy and security good than the thickness of cooling after the sensitization.Select big production capacity plastic film charge machine in addition in the sensitization powder charge system, improved production efficiency.
The above only is preferred embodiment of the present invention, not in order to restriction the present invention, all any modifications of being done within the spirit and principles in the present invention, is equal to and replaces and improvement etc., all should be included within protection scope of the present invention.
Claims (10)
1, a kind of emulsion explosive pharmacy and powder charge continuous production technology comprise the steps:
(1) prepares aqueous phase solution and oil-phase solution respectively;
(2) press processing compound, aqueous phase solution and oil-phase solution are conveyed into the mixing of colostrum device respectively, carry out colostrum, send into static mixer then and carry out the essence breast;
(3) the essence latex is sent into sensitization powder charge system and carried out sensitization processing back powder charge, after the cooling system cooling, deliver to packaging system again and pack.
2, continuous production technology according to claim 1 is characterized in that, described sensitization powder charge system is physical sensitization powder charge system, chemical sensitization powder charge system or physics, chemically composited sensitization powder charge system.
3, emulsion explosive pharmacy as claimed in claim 2 and powder charge continuous production technology is characterized in that, described physical sensitization powder charge system comprises perlite system or glass microballon system.
As continuous production technology as described in the claim 3, it is characterized in that 4, the physical sensitization powder charge system of smart latex through comprising described glass microballon system carries out sensitization and handle powder charge again, without described cooling system, directly delivers to packaging system and packs.
5, continuous production technology according to claim 1, it is characterized in that described aqueous phase solution is the ammonium nitrate solution of 87-92% concentration, described oil phase is made up of mineral oil and emulsifying agent, its mineral oil in fluid accounts for the 66.6%-91.6% of oil phase weight, and emulsifying agent accounts for the 8.4%-33.3% of oil phase weight.
As continuous production technology as described in the claim 5, it is characterized in that 6, processing compound is the 3-6% that oil-phase solution accounts for water, oil phase mixing solutions weight in the described step (2), aqueous phase solution accounts for the 94-97% of its weight.
7, continuous production technology according to claim 1 is characterized in that, described colostrum adopts the matrix spiral pump to carry, and described matrix spiral pump is provided with cutout dry grinding, overtemperature, superpressure safeguard protection deadman control, and rotating speed is lower than 200 rev/mins.
8, continuous production technology according to claim 1 is characterized in that the colostrum device is a small volume described in the described step (2), is no more than 120L colostrum device.
9, continuous production technology according to claim 1 is characterized in that, described charge machine adopts the plastic film charge machine.
10, as claim 1-9 continuous production technology as described in each, it is characterized in that latex is carried in the described step (3) under 88～92 ℃.
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN2007100753913A CN101357873B (en) | 2007-08-01 | 2007-08-01 | Continuous technique for preparing emulsifying explosive and charging |
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| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN2007100753913A CN101357873B (en) | 2007-08-01 | 2007-08-01 | Continuous technique for preparing emulsifying explosive and charging |
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| CN101357873A true CN101357873A (en) | 2009-02-04 |
| CN101357873B CN101357873B (en) | 2012-07-04 |
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Cited By (9)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN102603437A (en) * | 2012-02-28 | 2012-07-25 | 薛世忠 | Method for manufacturing emulsion explosive with swill-cooked dirty oil |
| CN103664424A (en) * | 2013-09-26 | 2014-03-26 | 石家庄成功机电有限公司 | Emulsion method and equipment for emulsion explosive |
| CN104058904A (en) * | 2014-07-07 | 2014-09-24 | 山东天宝化工股份有限公司 | Pilot test production line and production process of emulsion explosives |
| CN104502561A (en) * | 2014-11-24 | 2015-04-08 | 葛洲坝易普力股份有限公司 | Mixed explosive scientific research test platform |
| CN105272783A (en) * | 2015-11-10 | 2016-01-27 | 天津宏泰华凯科技有限公司 | Emulsification explosive-making system of emulsion explosive |
| CN105837387A (en) * | 2016-04-29 | 2016-08-10 | 安徽江南化工股份有限公司 | Anti-desensitization emulsified explosive and preparation method thereof |
| CN106081630A (en) * | 2016-08-11 | 2016-11-09 | 葛洲坝易普力四川爆破工程有限公司 | Glass microsphere induction system |
| CN110436205A (en) * | 2019-06-26 | 2019-11-12 | 新疆天河化工有限公司 | Large-diameter emulsified explosive conveying device and preparation method thereof |
| CN114591121A (en) * | 2022-03-15 | 2022-06-07 | 广东华威化工股份有限公司 | Emulsion explosive preparation method and system based on near infrared spectrum |
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2007
- 2007-08-01 CN CN2007100753913A patent/CN101357873B/en active Active
Cited By (14)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN102603437A (en) * | 2012-02-28 | 2012-07-25 | 薛世忠 | Method for manufacturing emulsion explosive with swill-cooked dirty oil |
| CN103664424B (en) * | 2013-09-26 | 2017-09-15 | 石家庄成功机电有限公司 | The emulsification method and equipment of a kind of emulsion |
| WO2015043140A1 (en) * | 2013-09-26 | 2015-04-02 | 石家庄成功机电有限公司 | Method and device for emulsifying emulsion explosive |
| CN103664424A (en) * | 2013-09-26 | 2014-03-26 | 石家庄成功机电有限公司 | Emulsion method and equipment for emulsion explosive |
| CN104058904A (en) * | 2014-07-07 | 2014-09-24 | 山东天宝化工股份有限公司 | Pilot test production line and production process of emulsion explosives |
| CN104058904B (en) * | 2014-07-07 | 2016-06-08 | 山东天宝化工股份有限公司 | A kind of emulsion pilot production line and production technology thereof |
| CN104502561A (en) * | 2014-11-24 | 2015-04-08 | 葛洲坝易普力股份有限公司 | Mixed explosive scientific research test platform |
| CN105272783A (en) * | 2015-11-10 | 2016-01-27 | 天津宏泰华凯科技有限公司 | Emulsification explosive-making system of emulsion explosive |
| CN105837387A (en) * | 2016-04-29 | 2016-08-10 | 安徽江南化工股份有限公司 | Anti-desensitization emulsified explosive and preparation method thereof |
| CN105837387B (en) * | 2016-04-29 | 2018-05-25 | 安徽江南化工股份有限公司 | A kind of anti-desensitization type emulsion and preparation method thereof |
| CN106081630A (en) * | 2016-08-11 | 2016-11-09 | 葛洲坝易普力四川爆破工程有限公司 | Glass microsphere induction system |
| CN110436205A (en) * | 2019-06-26 | 2019-11-12 | 新疆天河化工有限公司 | Large-diameter emulsified explosive conveying device and preparation method thereof |
| CN114591121A (en) * | 2022-03-15 | 2022-06-07 | 广东华威化工股份有限公司 | Emulsion explosive preparation method and system based on near infrared spectrum |
| CN114591121B (en) * | 2022-03-15 | 2022-11-15 | 广东华威化工股份有限公司 | Emulsion explosive preparation method and system based on near infrared spectrum |
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| Publication number | Publication date |
|---|---|
| CN101357873B (en) | 2012-07-04 |
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