CN1837164A - Powdered ammonium nitrate-fuel oil explosive and production process thereof - Google Patents
Powdered ammonium nitrate-fuel oil explosive and production process thereof Download PDFInfo
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- CN1837164A CN1837164A CN 200610039536 CN200610039536A CN1837164A CN 1837164 A CN1837164 A CN 1837164A CN 200610039536 CN200610039536 CN 200610039536 CN 200610039536 A CN200610039536 A CN 200610039536A CN 1837164 A CN1837164 A CN 1837164A
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- CN
- China
- Prior art keywords
- ammonium nitrate
- compound
- fuel oil
- explosive
- oil
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- Legal status (The legal status is an assumption and is not a legal conclusion. Google has not performed a legal analysis and makes no representation as to the accuracy of the status listed.)
- Granted
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- 239000002360 explosive Substances 0.000 title claims abstract description 40
- 239000000295 fuel oil Substances 0.000 title claims abstract description 30
- QGZKDVFQNNGYKY-UHFFFAOYSA-O Ammonium Chemical compound [NH4+] QGZKDVFQNNGYKY-UHFFFAOYSA-O 0.000 title claims abstract description 29
- 238000004519 manufacturing process Methods 0.000 title abstract description 8
- 150000001875 compounds Chemical class 0.000 claims abstract description 28
- 239000003921 oil Substances 0.000 claims abstract description 28
- 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 abstract description 23
- XLYOFNOQVPJJNP-UHFFFAOYSA-N water Substances O XLYOFNOQVPJJNP-UHFFFAOYSA-N 0.000 claims abstract description 22
- 239000000203 mixture Substances 0.000 claims abstract description 21
- 239000003795 chemical substances by application Substances 0.000 claims abstract description 16
- 238000002360 preparation method Methods 0.000 claims abstract description 13
- 238000001291 vacuum drying Methods 0.000 claims abstract description 5
- 238000003756 stirring Methods 0.000 claims abstract description 4
- 238000010438 heat treatment Methods 0.000 claims abstract description 3
- 239000001993 wax Substances 0.000 claims description 5
- 229920002907 Guar gum Polymers 0.000 claims description 4
- 229920000161 Locust bean gum Polymers 0.000 claims description 4
- 229910021538 borax Inorganic materials 0.000 claims description 4
- 239000002283 diesel fuel Substances 0.000 claims description 4
- 239000000665 guar gum Substances 0.000 claims description 4
- 235000010417 guar gum Nutrition 0.000 claims description 4
- 229960002154 guar gum Drugs 0.000 claims description 4
- 239000000711 locust bean gum Substances 0.000 claims description 4
- 235000010420 locust bean gum Nutrition 0.000 claims description 4
- 239000010721 machine oil Substances 0.000 claims description 4
- 239000012188 paraffin wax Substances 0.000 claims description 4
- KMUONIBRACKNSN-UHFFFAOYSA-N potassium dichromate Chemical compound [K+].[K+].[O-][Cr](=O)(=O)O[Cr]([O-])(=O)=O KMUONIBRACKNSN-UHFFFAOYSA-N 0.000 claims description 4
- 239000004328 sodium tetraborate Substances 0.000 claims description 4
- 235000010339 sodium tetraborate Nutrition 0.000 claims description 4
- 244000275012 Sesbania cannabina Species 0.000 claims description 3
- 238000005516 engineering process Methods 0.000 claims description 3
- 239000000463 material Substances 0.000 claims description 3
- 238000012423 maintenance Methods 0.000 claims description 2
- 239000003431 cross linking reagent Substances 0.000 abstract 2
- 239000002131 composite material Substances 0.000 abstract 1
- 239000000470 constituent Substances 0.000 abstract 1
- 238000001816 cooling Methods 0.000 abstract 1
- 230000003028 elevating effect Effects 0.000 abstract 1
- 238000004806 packaging method and process Methods 0.000 abstract 1
- 239000002002 slurry Substances 0.000 abstract 1
- 239000012071 phase Substances 0.000 description 17
- 238000005474 detonation Methods 0.000 description 8
- 238000000034 method Methods 0.000 description 6
- 239000007791 liquid phase Substances 0.000 description 5
- 238000004880 explosion Methods 0.000 description 4
- 238000002156 mixing Methods 0.000 description 4
- XGSVQGOPJUAOQH-UHFFFAOYSA-N aluminum;2-methyl-1,3,5-trinitrobenzene Chemical compound [Al+3].CC1=C([N+]([O-])=O)C=C([N+]([O-])=O)C=C1[N+]([O-])=O XGSVQGOPJUAOQH-UHFFFAOYSA-N 0.000 description 2
- 150000003863 ammonium salts Chemical class 0.000 description 2
- 238000004132 cross linking Methods 0.000 description 2
- 238000001035 drying Methods 0.000 description 2
- 239000000843 powder Substances 0.000 description 2
- 241000219782 Sesbania Species 0.000 description 1
- 230000009102 absorption Effects 0.000 description 1
- 238000010521 absorption reaction Methods 0.000 description 1
- 238000005422 blasting Methods 0.000 description 1
- 230000002950 deficient Effects 0.000 description 1
- 230000018044 dehydration Effects 0.000 description 1
- 238000006297 dehydration reaction Methods 0.000 description 1
- 238000011161 development Methods 0.000 description 1
- 239000006185 dispersion Substances 0.000 description 1
- 238000009775 high-speed stirring Methods 0.000 description 1
- 239000007788 liquid Substances 0.000 description 1
- 238000003672 processing method Methods 0.000 description 1
- 230000001007 puffing effect Effects 0.000 description 1
- 230000001846 repelling effect Effects 0.000 description 1
- 239000011435 rock Substances 0.000 description 1
- 230000001235 sensitizing effect Effects 0.000 description 1
- 239000008247 solid mixture Substances 0.000 description 1
- 239000007790 solid phase Substances 0.000 description 1
- 238000012360 testing method Methods 0.000 description 1
- 231100000167 toxic agent Toxicity 0.000 description 1
- 239000003440 toxic substance Substances 0.000 description 1
- 239000002023 wood Substances 0.000 description 1
Landscapes
- Liquid Carbonaceous Fuels (AREA)
Abstract
The invention discloses a powdered ammonium nitrate-fuel oil explosive and production process, wherein the constituents include (by weight ratio) ammonium nitrate 90-96%, composite oil phase 2.5-9%, cementing agent 0.1-1%, cross linking agent 0.05-0.5%, and the preparation process comprises the following steps, charging water into ammonium nitrate, dissolving and elevating temperature to 110-140 deg C, heating the compound oil phase to elevate the temperature to 85-120 deg. C, charging the cementing agent into dissolved ammonium nitrate solution, stirring at low speed, dispersing the compound oil phase into ammonium nitrate solution, charging cross linking agent, forming viscous slurry form mixture, carrying out vacuum drying, cooling down to below 40 deg C and packaging.
Description
Technical field
The present invention relates to a kind of ammonium nitrate-fuel oil mixture and preparation method thereof, particularly relate to a kind of powdered ammonium nitrate-fuel oil explosive and preparation method thereof.Can be used for the quick-fried industry explosive production of people producer and be used to produce powdered ammonium nitrate-fuel oil explosive, this explosive can be extensive use of in engineering explosion.
Background technology
Powder ammonium nitrate explosive is the industrial explosive kind of present usage quantity maximum, mainly contains an-tnt explosive and ammonium nitrate-fuel oil mixture two macrospecies.Generally speaking, an-tnt explosive contains high explosive sensitizing agent tritonal, and its blast performance is better than ammonium oils explosive, but tritonal is toxic substance, and is harmful, and the cost height.Ammonium oils explosive cost is low, and production technique is simple, but blast performance is poor, and easily oil impregnate is rotten, and storge quality is poor.Above-mentioned both equal easy moisture absorptions cakings, water repelling property difference and because explosion velocity is low be difficult to satisfy the requirement of hard rock blasting engineering, and production technique mostly is interruption technology greatly, the requirement of incompatibility Development of Industrial Explosives.
The solid-state ammonium nitrate of the most employing of common powdery ammonium nitrate-fuel oil or ammonium nitrate-fuel oil mixture and modified ammonium nitrate-fuel oil explosive mixes with liquid oil phase, this hybrid mode is difficult to oxygenant is uniformly dispersed with combustible agent and fully contact, thereby the prepared explosive detonation degree that reacts completely is limited, and blast performance is difficult to improve.
Chinese patent CN91107051.6 discloses a kind of bulking ammonium nitrate explosive, this explosive exists density on the low side, shortcomings such as the not high and water resisting property of unit volume power is not good, its production technique is made up of expanded operation and mixed pharmaceutical worker's preface, mixing pharmaceutical worker's preface is expanded ammonium nitrate and the solid phase of compound oil phase, wood powder and mixing of liquid phase, and detonation property is still not high.For this reason, Chinese patent CN1517325A discloses a kind of improved expanded ammonium nitrate again, its processing method is earlier to mix expanded with compound oil phase aqueous ammonium nitrate solution again, oxygenant and combustible agent are mixed between liquid phase and liquid phase, improve contact area, thereby improve detonation property, but this method has some not enough: the one, and water and oil phase requirement high-speed stirring, the 2nd, the very fast layering of oil phase and water in the puffing process, last oxygenant and combustible agent disperse inhomogeneous, also influence detonation property.
Summary of the invention
Purpose of the present invention is exactly at the above-mentioned defective that exists in the prior art, and a kind of have good detonation property and certain water resisting property are provided, and production technique is simple, is fit to the powdered ammonium nitrate-fuel oil explosive that serialization is produced.
Another object of the present invention provides the preparation method of above-mentioned powdered ammonium nitrate-fuel oil explosive.
For realizing the present invention's purpose, powdered ammonium nitrate-fuel oil explosive of the present invention is achieved through the following technical solutions.
The component of powdered ammonium nitrate-fuel oil explosive of the present invention comprises ammonium nitrate, compound oil phase, jointing compound, linking agent, and each component content (weight) scope is:
Ammonium nitrate 90%~96%;
Compound oil phase 2.5%~9%;
Jointing compound 0.1%~1%;
Linking agent 0.05%~0.5%.
Described compound oil phase can be compound wax, paraffin, machine oil, diesel oil and composition thereof; Described jointing compound is any or its mixture in sesbania gum, guar gum, the locust bean gum; Described linking agent is a kind of or mixture in potassium bichromate, the borax.
The preparation method of powdered ammonium nitrate-fuel oil explosive of the present invention is:
Industrial ammonium nitrate is added the water heating for dissolving be warmed up to 110 ℃~140 ℃; The compounded oil heat phase is warmed up to 85 ℃~120 ℃; Jointing compound is joined in the good ammonium nitrate solution of dissolving; Stirring at low speed is distributed to compound oil phase in the ammonium nitrate solution; Add linking agent, form the heavy-gravity paste mixture; Paste mixture is added in the vacuum tank, maintenance vacuum tightness-0.082MPa~-0.096MPa, carry out vacuum-drying; The exsiccant material is cooled to below 40 ℃ packs, promptly make powdered ammonium nitrate-fuel oil explosive of the present invention.
The water yield that adds in the preparation process is 3%~12% of each component gross weight of the present invention, and the water ratio in the finished product powdered ammonium nitrate-fuel oil explosive of the present invention is about 0.5%.
Principle of the present invention is: water and oil phase low speed are disperseed, make oil phase and water uniform mixing not stratified by crosslinking technological, through the vacuum-drying dehydration, form a kind of oil phase solid mixture mixed with water, thereby make powdered ammonium nitrate fuel oil mixture again.
The present invention has following remarkable advantage compared with prior art: oxygenant and combustible agent are to mix under the molecularity of liquid phase and liquid phase, owing to adopted crosslinking technological, oil phase and water remain good dispersion state in drying process, make explosive detonation characteristic significantly improve, explosion velocity 3700~4300m/s (φ 32mm), induced detonation 7~12cm, brisance 14~18mm, explosive have certain water resisting property.The preparation method is simple, has simplified mixed pharmaceutical worker room, is fit to serialization production.
Embodiment
For further describing the present invention, powdered ammonium nitrate-fuel oil explosive of the present invention and preparation method thereof is further described below in conjunction with embodiment.
According to table 1 preparation powdered ammonium nitrate-fuel oil explosive 100kg (according to dry basis).
Table 1 powdered ammonium nitrate-fuel oil explosive component and weight (kg)
Embodiment | Ammonium nitrate | Water | Compound wax | Paraffin | Machine oil or diesel oil | Sesbania gum | Guar gum | Locust bean gum | Potassium bichromate | Borax |
1 | 92.5 | 8 | 6 | 1.0 | 0.5 | |||||
2 | 91.47 | 9 | 8 | 0.5 | 0.03 | |||||
3 | 94.1 | 7.5 | 5 | 0.8 | 0.1 | |||||
4 | 94 | 7.5 | 5 | 0.8 | 0.2 | |||||
5 | 90 | 8 | 5 | 4 | 0.5 | 0.4 | 0.1 | |||
6 | 96 | 12 | 2.5 | 0.5 | 0.2 | 0.3 | 0.1 | 0.4 | ||
7 | 91.85 | 8 | 5 | 3 | 0.1 | 0.05 |
Annotate: because water is removed after drying, the ratio of water is for adding in the prescription, and all the other components amount to 100%.
The concrete operations step of embodiment 1-5 is:
The first step, the mixture that ammonium nitrate, water are formed is warmed up to 130 ℃, forms water;
Second step added jointing compound in water-phase material, stir;
In the 3rd step, compound wax is heated to 110 ℃;
The 4th step, the water and the oil phase mixing of preparation are stirred,
The 5th step is in the mixture with crosslinked adding oil phase and water;
The 6th the step, with the above-mentioned mixture that obtains through vacuum-drying (vacuum tightness-0.082~-0.096MPa), make powdered TNT-free modified ammonium nitrate-fuel oil explosive finished product.
Table 2 powdered ammonium nitrate-fuel oil explosive performance index
Index | Embodiment | Specification | Initial index | 1 month | 2 months | 3 months | 4 months | 5 months | 6 months |
Capacity for work (ml) | 1 | 32 | 328 | / | / | / | / | / | / |
2 | 325 | / | / | / | / | / | / | ||
3 | 345 | / | / | / | / | / | / | ||
4 | 338 | / | / | / | / | / | / | ||
5 | 320 | ||||||||
6 | 324 | ||||||||
7 | 321 | ||||||||
Explosion velocity (m/s) | 1 | 32 | 3685 | 3654 | 3560 | 3528 | 3525 | 3428 | 3420 |
2 | 3598 | 3580 | 3546 | 3513 | 3421 | 3415 | 3396 | ||
3 | 4223 | 4206 | 4189 | 4089 | 4078 | 4009 | 3985 | ||
4 | 4255 | 4215 | 4208 | 4150 | 4110 | 4000 | 3998 | ||
5 | 3556 | 3545 | 3525 | 3486 | 3425 | 3423 | 3405 | ||
6 | 3565 | 3546 | 3536 | 3512 | 3489 | 3456 | 3455 | ||
7 | 3525 | 3520 | 3510 | 3488 | 3456 | 3425 | 3398 | ||
Induced detonation (cm) | 1 | 32 | 9 | 9 | 8 | 8 | 7 | 6 | 5 |
2 | 9 | 8 | 8 | 7 | 6 | 6 | 5 | ||
3 | 10 | 9 | 8 | 8 | 7 | 6 | 6 | ||
4 | 9 | 8 | 7 | 6 | 5 | 5 | 5 | ||
5 | 7 | 7 | 7 | 6 | 6 | 5 | 5 | ||
6 | 7 | 7 | 7 | 6 | 6 | 6 | 6 | ||
7 | 7 | 7 | 6 | 6 | 5 | 5 | 5 | ||
Brisance (mm) | 1 | 32 | 15.65 | 15.38 | 15.24 | 15.15 | 14.26 | 14.00 | 13.98 |
2 | 16.21 | 16.06 | 15.96 | 15.59 | 15.28 | 15.15 | 15.03 | ||
3 | 15.99 | 15.56 | 15.36 | 14.86 | 14.58 | 14.44 | 14.25 | ||
4 | 16.21 | 15.89 | 15.31 | 15.25 | 14.75 | 14.66 | 14.35 | ||
5 | 15.26 | 15.05 | 14.96 | 14..85 | 14.69 | 14.58 | 14.25 | ||
6 | 15.05 | 14.88 | 14.75 | 14.56 | 14.05 | 14.01 | 13.96 | ||
7 | 14.95 | 14.75 | 14.26 | 14.28 | 14.12 | 13.87 | 13.56 |
The first step of embodiment 6 is warmed up to 140 ℃, and the 3rd step was warmed up to 85 ℃, and other step is identical with condition.
The first step of embodiment 7 is warmed up to 110 ℃, and the 3rd step was warmed up to 120 ℃, and other step is identical with condition.
After testing and store, record every index such as table 2.
Claims (6)
1. a powdered ammonium nitrate-fuel oil explosive is characterized in that comprising ammonium nitrate, compound oil phase, jointing compound, linking agent, and each component content (weight) scope is:
Ammonium nitrate 90%~96%;
Compound oil phase 2.5%~9%;
Jointing compound 0.1%~1%;
Linking agent 0.05%~0.5%.
2. powdered ammonium nitrate-fuel oil explosive as claimed in claim 1 is characterized in that: described compound oil phase can be compound wax, paraffin, machine oil, diesel oil and composition thereof.
3. powdered ammonium nitrate-fuel oil explosive as claimed in claim 1 or 2 is characterized in that: described jointing compound is any or its mixture in sesbania gum, guar gum, the locust bean gum.
4 powdered ammonium nitrate-fuel oil explosives as claimed in claim 1 or 2 is characterized in that: described linking agent is a kind of or mixture in potassium bichromate, the borax.
5. the preparation method of powdered ammonium nitrate-fuel oil explosive as claimed in claim 1 is characterized in that according to following technology: industrial ammonium nitrate is added the water heating for dissolving be warmed up to 110 ℃~140 ℃; The compounded oil heat phase is warmed up to 85 ℃~120 ℃; Jointing compound is joined in the good ammonium nitrate solution of dissolving; Stirring at low speed is distributed to compound oil phase in the ammonium nitrate solution; Add linking agent, form the heavy-gravity paste mixture; Paste mixture is added in the vacuum tank, maintenance vacuum tightness-0.082MPa~-0.096MPa, carry out vacuum-drying; The exsiccant material is cooled to below 40 ℃ packs, promptly make powdered ammonium nitrate-fuel oil explosive of the present invention.
6. the preparation method of powdered ammonium nitrate-fuel oil explosive as claimed in claim 5, it is characterized in that: described compound oil phase is compound wax, paraffin, machine oil, diesel oil and composition thereof, described jointing compound is any or its mixture in sesbania gum, guar gum, the locust bean gum, and described linking agent is a kind of or mixture in potassium bichromate, the borax.
Priority Applications (1)
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CNB200610039536XA CN100357234C (en) | 2006-04-14 | 2006-04-14 | Powdered ammonium nitrate-fuel oil explosive and production process thereof |
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CNB200610039536XA CN100357234C (en) | 2006-04-14 | 2006-04-14 | Powdered ammonium nitrate-fuel oil explosive and production process thereof |
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CN1837164A true CN1837164A (en) | 2006-09-27 |
CN100357234C CN100357234C (en) | 2007-12-26 |
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Cited By (3)
Publication number | Priority date | Publication date | Assignee | Title |
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CN113336611A (en) * | 2021-06-02 | 2021-09-03 | 石家庄成功机电有限公司 | Viscous explosive containing modified porous granular ammonium nitrate and preparation method thereof |
CN114315491A (en) * | 2022-01-18 | 2022-04-12 | 湖北东神天神实业有限公司 | Method for preparing powdery ammonium nitrate fuel oil explosive and product thereof |
CN115650809A (en) * | 2022-09-28 | 2023-01-31 | 安徽理工大学 | Colloidal ammonium amine explosive and preparation method thereof |
Family Cites Families (5)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
JPS57188489A (en) * | 1981-05-12 | 1982-11-19 | Nippon Oils & Fats Co Ltd | Water-in-oil emulsion explosive composition |
CN1032000A (en) * | 1987-09-14 | 1989-03-29 | 阜新矿务局十二厂 | Water gel explosives for mine |
CN1037090C (en) * | 1995-02-06 | 1998-01-21 | 南京理工大学 | Slurry explosive and mfg. method thereof |
FR2779426B1 (en) * | 1998-06-05 | 2000-07-13 | Poudres & Explosifs Ste Nale | SOLID PYROTECHNICAL CHARGES GAS GENERATORS BASED ON COMPOSITIONS CONTAINING WATER |
JP2001089285A (en) * | 1999-09-28 | 2001-04-03 | Asahi Kasei Corp | Granular explosive |
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2006
- 2006-04-14 CN CNB200610039536XA patent/CN100357234C/en not_active Expired - Fee Related
Cited By (4)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
CN113336611A (en) * | 2021-06-02 | 2021-09-03 | 石家庄成功机电有限公司 | Viscous explosive containing modified porous granular ammonium nitrate and preparation method thereof |
CN114315491A (en) * | 2022-01-18 | 2022-04-12 | 湖北东神天神实业有限公司 | Method for preparing powdery ammonium nitrate fuel oil explosive and product thereof |
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 |
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Effective date of registration: 20160812 Address after: 243031 rain Town, Ma'anshan City, Anhui Province Patentee after: Ma'anshan Jiangnan Chemical Co.,Ltd. Address before: 243100 Anhui province Dangtu County Department provided Road No. 10 Patentee before: Anhui Dun'an Chemical Industry Group Co.,Ltd. |
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