CN103012021A - Liquid distributing method and device for primary explosive production - Google Patents
Liquid distributing method and device for primary explosive production Download PDFInfo
- Publication number
- CN103012021A CN103012021A CN2012104789987A CN201210478998A CN103012021A CN 103012021 A CN103012021 A CN 103012021A CN 2012104789987 A CN2012104789987 A CN 2012104789987A CN 201210478998 A CN201210478998 A CN 201210478998A CN 103012021 A CN103012021 A CN 103012021A
- Authority
- CN
- China
- Prior art keywords
- liquid
- primary explosive
- priming explosive
- reactor
- solid
- 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.)
- Granted
Links
Images
Landscapes
- Physical Or Chemical Processes And Apparatus (AREA)
Abstract
The invention discloses a liquid distributing method and a liquid distributing device for primary explosive production. According to the method, the turbid liquid of the primary explosive is metered to realize the equivalent distribution of the solid primary explosive substance in the turbid liquid. The method mainly comprises the following steps in sequence: uniformly mixing the liquid with the solid primary explosive in a reacting kettle by stirring; and controlling the volume of drained turbid liquid through a flow sensor, thus controlling the quality of the solid primary explosive. Specific parameters are set for a stirrer in the reacting kettle, so that the solid and liquid substances are kept in a uniformly fixing state in the reacting kettle; and the flow sensor and a pneumatic valve are adopted and used for accomplishing the liquid distribution of the primary explosive. By adopting the liquid distributing method and the liquid distributing device for the primary explosive production, the primary explosive is kept in the uniform distribution state in the reacting kettle after the combination reaction, and therefore, the liquid distribution of the primary explosive can be realized, the technical problem that the primary explosive only can be distributed in an manual operation way can be solved, the automatic operation of the distribution process in the primary explosive production can be realized, an operator is prevented from directly contacting the dangerous goods, the problem due to drug floating can be avoided, and as a result, the potential risk is avoided.
Description
Technical field
The invention belongs to the industrial explosive material production technical field, relate to a kind of priming explosive production method, particularly relate to a kind of priming explosive and produce liquid minute dish method and device.
Background technology
Priming explosive is to be subject to outside energy excite and burn and can form rapidly a class sensitive explosive of detonation.Certain heat, electricity, light, mechanical equal excitation can have higher susceptibility to external world, and can export enough energy, ignite high explosive with detonation wave and cause detonation.Priming explosive is used widely in military, civilian a plurality of fields.The performance of priming explosive directly has influence on reliability and the security of priming system.The present priming explosive production unit of China is outmoded, and method is tradition comparatively also, mostly is manual operation, has serious potential safety hazard.With regard to minute dish operation in the current priming explosive production process, commonly used mainly contains two kinds, and the one, manually directly the priming explosive in the suction filtration tank is scooped out with spoon, be divided in each wooden capsule; The 2nd, by extraction plant with the priming explosive of suction filtration tank to around disperse the wooden capsule of manually again these priming explosives being packed into roughly.These methods the personnel that all cause directly contact with hazardous substance, has potential safety hazard.And, existing when manually scooping out priming explosive to spill phenomenon, the floating medicine that spills is difficult to collect this can bring potential safety hazard, also very easily its surrounding environment is polluted.
Summary of the invention
In order to solve the problems of the technologies described above, to the invention provides a kind of priming explosive and produce liquid minute dish method.
A kind of priming explosive is produced the method for liquid minute dish, by the metering to the priming explosive suspension liquid, realization divides dish to the equivalent of priming explosive solid matter in the suspension liquid, its main method is: make priming explosive solid and liquid mixing in the reactor even by stirring, utilize flow sensor control to emit the amount of suspension liquid, reach the purpose of control priming explosive solid masses, finish the equivalent of priming explosive under liquid state and divide dish.
Agitator in the described reactor is provided with specific parameter, guarantees that the solid-liquid thing is even admixture in reactor; Finish the liquid state of priming explosive by flow sensor, operated pneumatic valve and divide dish.
The special parameter of agitator setting is rotating speed in the described reactor, and its speed revolution value scope is 110~200r/min.
As another object of the present invention, provide a kind of priming explosive of realizing aforesaid method to produce liquid minute dish device, mainly comprise reactor, suction filtration drying tray, automatic delivering mechanism and support, described reactor is rack-mount, the suction filtration drying tray places on the automatic delivering mechanism, the outlet of reactor is corresponding with suction filtration drying tray upper end, is connected with flow sensor in the reactor exit, and flow sensor connects operated pneumatic valve.
The invention has the beneficial effects as follows:
Compared with prior art, the present invention is by setting the rotating speed of agitator in the reactor, make the state that in reactor, is evenly distributed after the priming explosive combination reaction, emit the amount of liquid by flow sensor control, liquid state in conjunction with operated pneumatic valve realization priming explosive is divided dish, changed and to have relied on manual operation just can finish minute present situation of dish in the existing priming explosive production, make priming explosive production realize automatization, not only improved production efficiency, also avoid personnel to contact with the direct of hazardous substance, solved the inhomogeneous problem of people's work point dish, eliminated safe hidden trouble and floating medicine hidden danger.
Description of drawings
Fig. 1 is liquid minute dish apparatus structure of the present invention schematic diagram.
Among the figure: 1-reactor, 2-suction filtration drying tray, 3-automatic delivering mechanism, 4-operated pneumatic valve, 5-flow sensor, 6-support.
Embodiment
Further describe technical scheme of the present invention below in conjunction with accompanying drawing, but that claimed scope is not limited to is described.
As shown in Figure 1, a kind of priming explosive is produced liquid minute dish method, make priming explosive solid and liquid mixing in the reactor 1 even by stirring, utilize flow sensor 5 controls to emit the amount of suspension liquid, reach the purpose of control priming explosive solid masses, agitator in the described reactor 1 is provided with specific parameter, guarantees that the solid-liquid thing is even admixture in reactor 1; Finish the liquid state of priming explosive by flow sensor 5, operated pneumatic valve 4 and divide dish.
Above-mentioned a kind of priming explosive is produced liquid minute dish method, and the special parameter of described reactor 1 interior agitator setting is rotating speed, and its speed revolution value scope is 110~200r/min.
As shown in Figure 1, a kind of priming explosive is produced liquid minute dish device, mainly comprise reactor 1, suction filtration drying tray 2, automatic delivering mechanism 3 and support 6, described reactor 1 is installed on the support 6, suction filtration drying tray 2 places on the automatic delivering mechanism 3, suction filtration drying tray 2 place reactor 1 outlet under, be connected with flow sensor 5 in reactor 1 exit, flow sensor 5 connects operated pneumatic valves 4.
By setting the rotating speed of agitator in the reactor, when the rotating speed of agitator is set to 110~200r/min, in reactor, evenly distribute solid, liquid body good mixing after can making the priming explosive combination reaction; Adopt flow sensor metering suspension liquid amount to come the equivalent blowing of liquid suspension liquid in the realization response still, in conjunction with operated pneumatic valve, divide the cooperation of coiling device by whole liquid state, can reach the purpose of control priming explosive solid masses.
Working process of the present invention is: at first priming explosive forms liquid suspension liquid after reactor 1 interior combination reaction, then operated pneumatic valve 4 is opened, flow sensor 5 begins to measure the suspension liquid amount from reactor 1 interior outflow, this suspension liquid flows into the suction filtration drying tray 2 that is arranged in reactor 1 bottom, reach predefined value such as liquid suspension liquid discharge, operated pneumatic valve 4 is closed, and then transfer roller is changed suction filtration drying tray 2, and final system reopens operated pneumatic valve 4 and enters next working cycle.
Claims (4)
1. a priming explosive is produced liquid minute dish method, it is characterized in that: by the metering to the priming explosive suspension liquid, realization divides dish to the equivalent of priming explosive solid matter in the suspension liquid, its main method is: make priming explosive solid and liquid mixing in the reactor (1) even by stirring, utilize flow sensor (5) control to emit the amount of suspension liquid, reach the purpose of control priming explosive solid masses, finish the equivalent of priming explosive under liquid state and divide dish.
2. a kind of priming explosive according to claim 1 is produced liquid minute dish method, it is characterized in that: the agitator in the described reactor (1) is provided with specific parameter, guarantees that the solid-liquid thing is even admixture in reactor (1); Finish the liquid state of priming explosive by flow sensor (5), operated pneumatic valve (4) and divide dish.
3. a kind of priming explosive according to claim 1 is produced liquid minute dish method, and it is characterized in that: the special parameter of the interior agitator setting of described reactor (1) is rotating speed, and its speed revolution value scope is 110~200r/min.
4. a liquid state that realizes the liquid minute dish method of as claimed in claim 1 priming explosive production is divided the dish device, mainly comprise reactor (1), suction filtration drying tray (2), automatic delivering mechanism (3) and support (6), it is characterized in that: described reactor (1) is installed on the support (6), suction filtration drying tray (2) places on the automatic delivering mechanism (3), the outlet of reactor (1) is corresponding with suction filtration drying tray (2) upper end, be connected with flow sensor (5) in reactor (1) exit, flow sensor (5) connects operated pneumatic valve (4).
Priority Applications (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
CN201210478998.7A CN103012021B (en) | 2012-11-22 | 2012-11-22 | Liquid distributing method and device for primary explosive production |
Applications Claiming Priority (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
CN201210478998.7A CN103012021B (en) | 2012-11-22 | 2012-11-22 | Liquid distributing method and device for primary explosive production |
Publications (2)
Publication Number | Publication Date |
---|---|
CN103012021A true CN103012021A (en) | 2013-04-03 |
CN103012021B CN103012021B (en) | 2015-04-22 |
Family
ID=47961189
Family Applications (1)
Application Number | Title | Priority Date | Filing Date |
---|---|---|---|
CN201210478998.7A Active CN103012021B (en) | 2012-11-22 | 2012-11-22 | Liquid distributing method and device for primary explosive production |
Country Status (1)
Country | Link |
---|---|
CN (1) | CN103012021B (en) |
Cited By (2)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
CN105315112A (en) * | 2015-11-17 | 2016-02-10 | 上海桥键能源科技有限公司 | Full-automatic integrated production device for initiating explosive |
CN109369310A (en) * | 2018-12-24 | 2019-02-22 | 长沙学院 | A kind of gunpowder quantifies mixing arrangement |
Citations (4)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
WO1998040308A2 (en) * | 1997-03-14 | 1998-09-17 | The Coca-Cola Company | Postmix beverage dispenser |
CN202089753U (en) * | 2011-01-27 | 2011-12-28 | 魏文贞 | Fluid distributing machine |
CN202297085U (en) * | 2011-09-09 | 2012-07-04 | 泸州市慧江机械制造有限公司 | Quantitative filling machine |
CN203048827U (en) * | 2012-11-22 | 2013-07-10 | 贵州久联民爆器材发展股份有限公司 | Liquid state dividing device for production of initiating explosive |
-
2012
- 2012-11-22 CN CN201210478998.7A patent/CN103012021B/en active Active
Patent Citations (4)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
WO1998040308A2 (en) * | 1997-03-14 | 1998-09-17 | The Coca-Cola Company | Postmix beverage dispenser |
CN202089753U (en) * | 2011-01-27 | 2011-12-28 | 魏文贞 | Fluid distributing machine |
CN202297085U (en) * | 2011-09-09 | 2012-07-04 | 泸州市慧江机械制造有限公司 | Quantitative filling machine |
CN203048827U (en) * | 2012-11-22 | 2013-07-10 | 贵州久联民爆器材发展股份有限公司 | Liquid state dividing device for production of initiating explosive |
Cited By (3)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
CN105315112A (en) * | 2015-11-17 | 2016-02-10 | 上海桥键能源科技有限公司 | Full-automatic integrated production device for initiating explosive |
CN105315112B (en) * | 2015-11-17 | 2018-02-02 | 上海桥键能源科技有限公司 | A kind of integrated full automatic production equipment of priming |
CN109369310A (en) * | 2018-12-24 | 2019-02-22 | 长沙学院 | A kind of gunpowder quantifies mixing arrangement |
Also Published As
Publication number | Publication date |
---|---|
CN103012021B (en) | 2015-04-22 |
Similar Documents
Publication | Publication Date | Title |
---|---|---|
CN203048827U (en) | Liquid state dividing device for production of initiating explosive | |
CN104084079A (en) | Mixing device of anhydrous sodium sulfate used for dye | |
CN201832569U (en) | Automatic dispensing device of powder | |
CN103012021B (en) | Liquid distributing method and device for primary explosive production | |
CN204320115U (en) | Mixed stirring device smashed to pieces by analytical chemistry material | |
CN103920409A (en) | Online automatic preparation addition equipment for solid PAM (polyacrylamide) agent | |
CN102327751B (en) | Three-cavity dosing device for sewage treatment and dosing method thereof | |
CN203754622U (en) | Device for automatically screening and packing initiating explosive | |
CN203678304U (en) | Pill sugar coating slurry premixing device | |
CN105817159A (en) | Full-automatic blending device for flame-retarding and explosion-suppression diesel oil production | |
CN202078871U (en) | Constant-temperature high-pressure stirring and injecting device | |
CN203715534U (en) | Initiating explosive production device | |
CN203540388U (en) | Batching device for coating machine | |
CN208642395U (en) | A kind of Chemical Manufacture mixing arrangement with dual filtering functions | |
CN103831055B (en) | A kind of mixing procedure of pearl stone sound absorbing baffle raw material and equipment | |
CN203602522U (en) | Device for constant-volume distribution of solid substances in turbid liquid | |
CN204768388U (en) | Automatic medicine medicine machine that dissolves of sewage treatment | |
CN205627739U (en) | A full -automatic blending device that is used for fire -retardant datonation -inhibition diesel oil production | |
CN208449267U (en) | A kind of macromolecule polymer solution continuous preparation device | |
CN204147871U (en) | A kind of novel concrete grinding aid production line | |
CN208018446U (en) | A kind of layering solidliquid mixture uniform conveying control device online | |
CN203874705U (en) | On-line automatic dispensing and feeding equipment for PAM solid medicament | |
CN203048826U (en) | Suction filtering, drying and explosive containing tray used for production of primary explosives | |
CN208586064U (en) | Continuous full-automatic dry powder chemicals dosing plant | |
CN216900063U (en) | Medicine component detection device |
Legal Events
Date | Code | Title | Description |
---|---|---|---|
C06 | Publication | ||
PB01 | Publication | ||
C10 | Entry into substantive examination | ||
SE01 | Entry into force of request for substantive examination | ||
C14 | Grant of patent or utility model | ||
GR01 | Patent grant | ||
CP03 | Change of name, title or address | ||
CP03 | Change of name, title or address |
Address after: 550000 Xintian Park, high tech Industrial Development Zone, Guiyang City, Guizhou Province Patentee after: Poly United Chemical Holding Group Co., Ltd Address before: 550001, Guiyang 372 North Road, Guizhou, Guizhou daily 18 floor, long union Technology Center, Baoshan Patentee before: GUIZHOU JIULIAN INDUSTRIAL EXPLOSIVE MATERIALS DEVELOPMENT Co.,Ltd. |