CN205856344U - High density bulking ammonium oil explosive-source explosive post production line - Google Patents
High density bulking ammonium oil explosive-source explosive post production line Download PDFInfo
- Publication number
- CN205856344U CN205856344U CN201620832189.5U CN201620832189U CN205856344U CN 205856344 U CN205856344 U CN 205856344U CN 201620832189 U CN201620832189 U CN 201620832189U CN 205856344 U CN205856344 U CN 205856344U
- Authority
- CN
- China
- Prior art keywords
- explosive
- oil
- oil phase
- ammonium
- storage tank
- Prior art date
- 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.)
- Active
Links
Abstract
High density bulking ammonium oil explosive-source explosive post production line, it includes disintegrating machine (1), ammonium nitrate melting tank (2), ammonium nitrate solution aqueous phase storage tank (3), oil phase melting tank (4), oil phase storage tank (5), water oil phase mixing agitator (6), screw pump (7), expanded ammonium oil crystallizer (8), explosive cooling machine (9), wood powder metered charge machine (10), semi-finished product conveying worm (12) and finished product bin (13).This utility model advantage is: explosive-source explosive post degree of packing is big, and explosion velocity powder charge hygroscopicity high, interior is little, and the toxic and harmful amount that explosion produces is little.
Description
Technical field
This utility model relates to nitrolite manufacture, explosive-source explosive post manufacturing technology field, is specifically related to high density bulking ammonium
Oil explosive-source explosive post production line.
Background technology
At present, expanded ammonium nitrate explosive-source explosive post production line be by use expanded ammonium nitrate commercial explosive be that interior powder charge prepares, nitric acid
Ammonium, swelling agent aqueous solution carry out expanded formation expanded ammonium nitrate, add a certain proportion of composite oil phase, wood powder or blast reducer mixing
After the interior powder charge of bulking ammonium nitrate explosive made, then make expanded ammonium nitrate focus by explosive-source explosive post charging machine, sealing machine, stamp
Powder column.Existing expanded ammonium nitrate explosive-source explosive post Technology, degree of packing is little, product explosion velocity powder charge anti-moisture absorption property the highest, interior
Power is weak, and the toxic and harmful amount that explosion produces is big.
Utility model content
The purpose of this utility model is aiming at present, and expanded ammonium nitrate explosive-source explosive post production line is by using expanded ammonium nitrate work
Industry explosive is that interior powder charge prepares, and ammonium nitrate, swelling agent aqueous solution carry out expanded formation expanded ammonium nitrate, add a certain proportion of multiple
The interior powder charge of the bulking ammonium nitrate explosive made after closing oil phase, wood powder or blast reducer mixing, then by explosive-source explosive post charging machine, sealing
Machine, stamp make expanded ammonium nitrate explosive-source explosive post.Existing expanded ammonium nitrate explosive-source explosive post Technology, degree of packing is little, and product is quick-fried
Speed powder charge the highest, interior anti-moisture absorption property power is weak, the deficiency that the toxic and harmful amount that explosion produces is big, and utility model high density
Expanded ammonium oil explosive-source explosive post production line.
This utility model high density bulking ammonium oil explosive-source explosive post production line, it includes disintegrating machine, ammonium nitrate melting tank, nitric acid
Ammonium salt solution aqueous phase storage tank, oil phase melting tank, oil phase storage tank, water oil phase mixing agitator, screw pump, expanded ammonium oil crystallizer, cool
Medicine machine, wood powder metered charge machine, semi-finished product conveying worm and finished product bin, the discharging opening of disintegrating machine and ammonium nitrate melting tank
Charging aperture communicates, and the discharging opening of ammonium nitrate melting tank communicates with the charging aperture of ammonium nitrate solution aqueous phase storage tank, oil phase melting tank
Discharging opening communicates with the charging aperture of oil phase storage tank, the discharging opening of ammonium nitrate solution aqueous phase storage tank and oil phase storage tank respectively with water oil phase
The charging aperture of mixing agitator communicates, and the discharging opening of water oil phase mixing agitator is entered by screw pump and expanded ammonium oil crystallizer
Material mouth communicates, and the discharging opening of expanded ammonium oil crystallizer and wood powder metered charge machine communicates with the charging aperture of explosive cooling machine respectively, the medicine of a cold nature
The discharging opening of machine is communicated with the charging aperture of finished product bin by semi-finished product conveying worm.
This utility model advantage is: explosive-source explosive post degree of packing is big, and explosion velocity powder charge hygroscopicity high, interior is little, and explosion produces
Toxic and harmful amount is little.
Accompanying drawing explanation
Fig. 1 is this utility model structural representation.
Detailed description of the invention
As it is shown in figure 1, this utility model explosive-source explosive post high density bulking ammonium oil production line, molten including disintegrating machine 1, ammonium nitrate
Change tank 2, ammonium nitrate solution aqueous phase storage tank 3, oil phase melting tank 4, oil phase storage tank 5, water oil phase mixing agitator 6, screw pump 7, swollen
Change ammonium oil crystallizer 8, explosive cooling machine 9, wood powder metered charge machine 10, semi-finished product conveying worm 12 and finished product bin 13, disintegrating machine 1
Discharging opening and the charging aperture of ammonium nitrate melting tank 2 communicate, the discharging opening of ammonium nitrate melting tank 2 and ammonium nitrate solution aqueous phase storage tank
The charging aperture of 3 communicates, and the discharging opening of oil phase melting tank 4 communicates with the charging aperture of oil phase storage tank 5, ammonium nitrate solution aqueous phase storage tank 3
Charging aperture with water oil phase mixing agitator 6 communicates respectively with the discharging opening of oil phase storage tank 5, going out of water oil phase mixing agitator 6
Material mouth is communicated by the charging aperture of screw pump 7 with expanded ammonium oil crystallizer 8, expanded ammonium oil crystallizer 8 and wood powder metered charge machine
The discharging opening of 10 charging aperture with explosive cooling machine 9 respectively communicates, and the discharging opening of explosive cooling machine 9 is by semi-finished product conveying worm 12 and becomes
The charging aperture of product feed bin 13 communicates.
High density bulking ammonium oil explosive-source explosive post production line described in utilization prepares the side of high density bulking ammonium oil explosive-source explosive post
Method is:
1. dissolving at ammonium nitrate melting tank 2 after ammonium nitrate being crushed by disintegrating machine 1, prepared ammonium nitrate solution puts into nitric acid
In ammonium salt solution aqueous phase storage tank 3；
2., after composite oil phase being dissolved in oil phase melting tank 4, put in oil phase storage tank 5；
3. the ammonium nitrate solution in ammonium nitrate solution aqueous phase storage tank 3 is oily at water with the liquid compound oil in oil phase storage tank 5
It is stirred mixing in phase mixing agitator 6 and obtains expanded ammonium oil matrix；
4. vacuum crystallization is carried out in expanded ammonium oil matrix being transported to expanded ammonium oil crystallizer 8 by screw pump 7；
5. the crystalline solid in expanded ammonium oil crystallizer 8 and the wood powder in wood powder metered charge machine 10 by weight percentage
97%～95%, 3%～5% put into explosive cooling machine 9 in carry out combination cooling；
6. the mixture after cooling is transported through in being transported to finished product bin 13 by semi-finished product conveying worm 12, in shake
High explosion-speed seismic explosive columns is made in powder column worker-house, source, and semi-finished product conveying worm 12 is the most further mixed conveying when
Close.
It is provided with aqueous phase mistake between discharging opening and the charging aperture of water oil phase mixing agitator 6 of ammonium nitrate solution aqueous phase storage tank 3
Filter 3-1, is provided with oil phase filter 3-2 between discharging opening and the charging aperture of water oil phase mixing agitator 6 of oil phase storage tank 5
It is provided with pan 6-1 between discharging opening and the charging aperture of screw pump 7 of water oil phase mixing agitator 6.
Working method and principle: dissolve at ammonium nitrate melting tank 2 after ammonium nitrate is crushed by disintegrating machine 1, prepare nitric acid
Ammonium salt solution is put in ammonium nitrate solution aqueous phase storage tank 3, after composite oil phase is dissolved in oil phase melting tank 4, puts into oil phase storage tank 5
In, the ammonium nitrate solution in ammonium nitrate solution aqueous phase storage tank 3 and the liquid compound oil in oil phase storage tank 5 are at water oil phase mix and blend
Being stirred mixing in device 6 and obtain expanded ammonium oil matrix, the discharging opening of aqueous phase storage tank 3 is provided with aqueous phase filter 3-1, oil phase storage tank
The discharging opening of 5 is provided with oil phase filter 3-2, it is to avoid impurity enters in water oil phase mixing agitator 6.Expanded ammonium oil matrix passes through
Screw pump 7 carries out expanded crystallization in being transported to expanded ammonium oil crystallizer 8, pan 6-1 avoid in expanded ammonium oil matrix at impurity
Enter in expanded ammonium oil crystallizer 8, owing to liquid compound oil needs to be maintained at 90-100 DEG C, the expanded ammonium oil base therefore obtained
Matter temperature is higher, and expanded ammonium oil matrix temperature after expanded crystallizer 8 intercrystalline is higher, carries out in needing to enter into explosive cooling machine 9
Cooling, mixes with expanded ammonium oil crystal in the wood powder in wood powder metered charge machine 10 being added to explosive cooling machine 9 while cooling
Closing, crystalline solid and wood powder are 97%～95% and 3%～5% by weight percentage, and the expanded ammonium oil crystal after cooling is together with wood powder
It is transported in finished product bin 13 by semi-finished product conveying worm 12, to swollen during semi-finished product conveying worm 12 carries
Changing ammonium oil crystal and wood powder further mixes, improve density and the stability of expanded ammonium oil, finished product bin 13 is by being transported to
Explosive-source explosive post worker-house carries out powder charge, gland, stamp, makes high density (explosion velocity) expanded ammonium oil explosive-source explosive post.
Claims (1)
1. high density bulking ammonium oil explosive-source explosive post production line, it is characterised in that it include disintegrating machine (1), ammonium nitrate melting tank (2),
Ammonium nitrate solution aqueous phase storage tank (3), oil phase melting tank (4), oil phase storage tank (5), water oil phase mixing agitator (6), screw pump
(7), expanded ammonium oil crystallizer (8), explosive cooling machine (9), wood powder metered charge machine (10), semi-finished product conveying worm (12) and finished product
Feed bin (13), the discharging opening of disintegrating machine (1) and the charging aperture of ammonium nitrate melting tank (2) communicate, the discharging of ammonium nitrate melting tank (2)
Mouth communicates with the charging aperture of ammonium nitrate solution aqueous phase storage tank (3), and the discharging opening of oil phase melting tank (4) enters with oil phase storage tank (5)
Material mouth communicate, the discharging opening of ammonium nitrate solution aqueous phase storage tank (3) and oil phase storage tank (5) respectively with water oil phase mixing agitator (6)
Charging aperture communicate, the discharging opening of water oil phase mixing agitator (6) is entered by screw pump (7) and expanded ammonium oil crystallizer (8)
Material mouth communicates, the discharging opening of expanded ammonium oil crystallizer (8) and wood powder metered charge machine (10) respectively with the charging aperture of explosive cooling machine (9)
Communicating, the discharging opening of explosive cooling machine (9) is communicated by the charging aperture of semi-finished product conveying worm (12) with finished product bin (13).
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201620832189.5U CN205856344U (en) | 2016-08-03 | 2016-08-03 | High density bulking ammonium oil explosive-source explosive post production line |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201620832189.5U CN205856344U (en) | 2016-08-03 | 2016-08-03 | High density bulking ammonium oil explosive-source explosive post production line |
Publications (1)
| Publication Number | Publication Date |
|---|---|
| CN205856344U true CN205856344U (en) | 2017-01-04 |
Family
ID=57654665
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| CN201620832189.5U Active CN205856344U (en) | 2016-08-03 | 2016-08-03 | High density bulking ammonium oil explosive-source explosive post production line |
Country Status (1)
| Country | Link |
|---|---|
| CN (1) | CN205856344U (en) |
Cited By (2)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN106554241A (en) * | 2016-08-03 | 2017-04-05 | 湖北凯龙化工集团股份有限公司 | High density bulking ammonium oil explosive-source explosive post production line and production method |
| CN113788731A (en) * | 2021-09-30 | 2021-12-14 | 中国人民解放军国防科技大学 | Automatic production line for elastic glue |
-
2016
- 2016-08-03 CN CN201620832189.5U patent/CN205856344U/en active Active
Cited By (2)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN106554241A (en) * | 2016-08-03 | 2017-04-05 | 湖北凯龙化工集团股份有限公司 | High density bulking ammonium oil explosive-source explosive post production line and production method |
| CN113788731A (en) * | 2021-09-30 | 2021-12-14 | 中国人民解放军国防科技大学 | Automatic production line for elastic glue |
Similar Documents
| Publication | Publication Date | Title |
|---|---|---|
| CN205856344U (en) | High density bulking ammonium oil explosive-source explosive post production line | |
| CN101423448B (en) | Low detonation velocity powdery emulsifying explosive | |
| CN104045495B (en) | Granular ammonium nitrate-fuel oil mixture of a kind of viscosity and preparation method thereof | |
| CN102515988A (en) | Method for preparation of emulsion explosive by using waste explosives | |
| CN205308199U (en) | It uses agitating unit to contain production of water -soluble fertilizer of rotten phytic acid of high concentration | |
| CN105367818B (en) | A kind of production method preparing sterling nylon 6 with nylon 6 waste material for raw material | |
| CN106748596B (en) | A kind of viscous explosive and preparation method thereof of no single chmical compound explosive | |
| CN102675005A (en) | Emulsion explosive used in deep water blasting and preparation method thereof | |
| CN101823926A (en) | Preparation process of emulsion explosive | |
| CN104262067B (en) | The heat-sensitized method preparing emulsion explosive | |
| CN106008122B (en) | One kind is for on-site mixed powdery emulsifying explosive and preparation method thereof | |
| CN102503742A (en) | Three-grade coal mine allowable emulsified explosive and preparation method thereof | |
| CN105712809A (en) | High-temperature-sensitized emulsion explosive and preparation method thereof | |
| CN104743580B (en) | A kind of extract the method reclaiming salt lake tail salt, leaving over potassium chloride in useless carnallite | |
| CN102424644B (en) | Expanded ammonium nitrate and preparation method thereof | |
| CN106554241A (en) | High density bulking ammonium oil explosive-source explosive post production line and production method | |
| CN201825886U (en) | Continuous expanded ammonium nitrate explosive mixing device | |
| CN102285848A (en) | Pressure-resistant high-power emulsified seismic explosive column and preparation method thereof | |
| CN104030752A (en) | Production method of water-soluble fertilizer containing trace elements | |
| CN105271125B (en) | A kind of spherical shape potassium hyperchlorate production technology | |
| CN105461495A (en) | Continuous production process for powdery industrial explosive for metal explosion cladding | |
| CN103396272A (en) | Method for recycling waste emulsion explosive in rock powder emulsion explosive | |
| CN106586968A (en) | Safe extracting method of ammonium perchlorate in solid FAE (Fuel Air Explosive) | |
| CN1137071C (en) | Process for preparing loose ammonium nitrate crystals using anti-hardening agent | |
| CN105819405A (en) | Sulfur putting method in thionyl chloride refining process |
Legal Events
| Date | Code | Title | Description |
|---|---|---|---|
| C14 | Grant of patent or utility model | ||
| GR01 | Patent grant |