CN203904239U - Conveying device for material mixing in emulsion explosive production - Google Patents
Conveying device for material mixing in emulsion explosive production Download PDFInfo
- Publication number
- CN203904239U CN203904239U CN201420338952.XU CN201420338952U CN203904239U CN 203904239 U CN203904239 U CN 203904239U CN 201420338952 U CN201420338952 U CN 201420338952U CN 203904239 U CN203904239 U CN 203904239U
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- Prior art keywords
- oil phase
- water
- conveying device
- compressed air
- control valve
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- 238000004519 manufacturing process Methods 0.000 title claims abstract description 24
- 239000000839 emulsion Substances 0.000 title claims abstract description 20
- 239000002360 explosive Substances 0.000 title claims abstract description 16
- 239000000463 material Substances 0.000 title claims abstract description 13
- XLYOFNOQVPJJNP-UHFFFAOYSA-N water Substances O XLYOFNOQVPJJNP-UHFFFAOYSA-N 0.000 claims abstract description 55
- 230000003068 static effect Effects 0.000 claims abstract description 34
- 230000001105 regulatory effect Effects 0.000 claims abstract description 18
- 230000001235 sensitizing effect Effects 0.000 claims abstract description 18
- 239000012071 phase Substances 0.000 claims description 55
- 206010070834 Sensitisation Diseases 0.000 claims description 20
- 230000008313 sensitization Effects 0.000 claims description 20
- 239000003795 chemical substances by application Substances 0.000 claims description 16
- 230000001804 emulsifying effect Effects 0.000 claims description 13
- 239000008346 aqueous phase Substances 0.000 claims description 5
- 239000003995 emulsifying agent Substances 0.000 abstract 2
- 238000002360 preparation method Methods 0.000 abstract 2
- 238000005516 engineering process Methods 0.000 description 6
- 239000011159 matrix material Substances 0.000 description 5
- 238000000034 method Methods 0.000 description 4
- 230000006835 compression Effects 0.000 description 2
- 238000007906 compression Methods 0.000 description 2
- 238000004945 emulsification Methods 0.000 description 2
- 239000007788 liquid Substances 0.000 description 2
- 238000005086 pumping Methods 0.000 description 2
- 230000000630 rising effect Effects 0.000 description 2
- 230000003245 working effect Effects 0.000 description 2
- 238000001816 cooling Methods 0.000 description 1
- 230000000694 effects Effects 0.000 description 1
- 238000004880 explosion Methods 0.000 description 1
- 239000000203 mixture Substances 0.000 description 1
- 239000000843 powder Substances 0.000 description 1
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- Liquid Carbonaceous Fuels (AREA)
- Accessories For Mixers (AREA)
- Colloid Chemistry (AREA)
Abstract
The utility model discloses a conveying device for material mixing in emulsion explosive production, aiming to provide a conveying device having high production safety. The conveying device comprises a water phase conveying device, an oil phase conveying device, a sensitizer conveying device, a static emulsifier and a static sensitizing disperser; the water phase conveying device consists of a water phase preparation tank, a water phase conveying pump, a one-way control valve I, a water phase intermediate tank, a one-way control valve II, a water phase storage tank, a water phase flow regulating valve and a water phase flowmeter which are sequentially connected; the oil phase conveying device consists of an oil phase preparation tank, an oil phase conveying pump, a one-way control valve III, an oil phase intermediate tank, an one-way control valve IV, an oil phase storage tank, an oil phase flow regulating valve and an oil phase flowmeter which are sequentially connected; the sensitizer conveying device consists of a sensitizer storage tank, a sensitizer conveying pump and a sensitizer flowmeter which are connected sequentially; the water phase flowmeter, the oil phase flowmeter and the sensitizer flowmeter are connected; the sensitizer flowmeter, the static emulsifier and the static sensitizing disperser are connected.
Description
Technical field
The utility model relates to emulsion explosive production equipment technical field, especially relates to a kind of e Foerderanlage for emulsion explosive production mixing of materials.
Background technology
Current emulsion explosive production line employed both at home and abroad, all be unable to do without the rotating machinerys such as high-pressure delivery pump (moisture, oil phase transferpump and/or matrix transferpump) and emulsification, sensitization, that this kind equipment not only consumes energy is high, noise is large, be mainly to have great potential safety hazard, cause explosion hazard in recent years to take place frequently.Although some manufacturers have adopted static emulsion, static sensitization production technique, because water, oil phase transferpump pressure are higher, there is larger potential safety hazard in production process, and equipment fragile all the time.
Summary of the invention
The utility model has overcome shortcoming of the prior art, and the e Foerderanlage for emulsion explosive production mixing of materials that a kind of production security is high, can be continuously produced is provided.
In order to solve the problems of the technologies described above, the utility model is achieved through the following technical solutions: a kind of e Foerderanlage for emulsion explosive production mixing of materials, comprises water conveying device, oil phase e Foerderanlage, sensitizer conveying device, static emulsifying apparatus and static sensitization decollator;
Described water conveying device comprises the water preparing tank, water conveying pump, one-way control valve one, water tundish, one-way control valve two, water storage tank, aqueous phase stream adjustable valve and the water under meter that connect successively; Described water under meter is connected with described static emulsifying apparatus; Described water tundish are communicated with compressed air source by compressed air regulating valve one, and described water storage tank is communicated with compressed air source by compressed air regulating valve two;
Described oil phase e Foerderanlage comprises the oil phase preparing tank, oil phase transferpump, one-way control valve three, oil phase tundish, one-way control valve four, oil phase storage tank, oil phase flow control valve and the oil phase under meter that connect successively; Described oil phase under meter is connected with described static emulsifying apparatus; Described oil phase tundish are by compressed air regulating valve tee joint compressed air source, and described oil phase storage tank is communicated with compressed air source by compressed air regulating valve four;
Described sensitizer conveying device comprises the sensitizing agent storage tank, sensitizing agent transferpump and the sensitizing agent under meter that connect successively; Described sensitizing agent under meter is connected with described static sensitization decollator;
Described static emulsifying apparatus is connected with described static sensitization decollator.
Preferably, described static sensitization decollator connects filling apparatus.
Preferably, the air pressure of described compressed air source is 0.2～1.8 MPa.
Compared with prior art, the utlity model has following advantage:
(1) the utility model is a kind of anhydrous, oil phase high-pressure delivery pump and matrix transferpump, meets the e Foerderanlage that the emulsion explosive serialization of industry technology developing direction is produced, the aqueous phase solution of this e Foerderanlage, oil-phase solution all adopt pressurized air as transmitting power, thoroughly eradicate the potential safety hazard of high pressure pumping, promote greatly the level of emulsion explosive production line safety in production, and compressed air delivery is impacted little to equipment, the effectively work-ing life of extension device.
(2) e Foerderanlage of the present utility model had both been applicable to first cooling rear sensitization production technique, was also applicable to cooling-production technology after first sensitization, and suitability is stronger.Adopt static emulsion, static sensitization technology, without the rotating machinery such as emulsification, sensitization, there is noise little, the advantage that service life of equipment is long.
Brief description of the drawings
In order to be illustrated more clearly in the utility model embodiment or technical scheme of the prior art, to the accompanying drawing of required use in embodiment or description of the Prior Art be briefly described below, apparently, accompanying drawing in the following describes is only embodiment more of the present utility model, for those of ordinary skill in the art, do not paying under the prerequisite of creative work, can also obtain according to these accompanying drawings other accompanying drawing.
Fig. 1 is structural representation of the present utility model.
Embodiment
Below in conjunction with the accompanying drawing in the utility model embodiment, the technical scheme in the utility model embodiment is clearly and completely described, obviously, described embodiment is only the utility model part embodiment, instead of whole embodiment.Based on the embodiment in the utility model, those of ordinary skill in the art are not paying the every other embodiment obtaining under creative work prerequisite, all belong to the scope of the utility model protection.
Shown in Fig. 1, for the e Foerderanlage of emulsion explosive production mixing of materials, comprise water conveying device 30, oil phase e Foerderanlage 40, sensitizer conveying device 50, static emulsifying apparatus 24 and static sensitization decollator 25;
Described water conveying device 30 comprises the water preparing tank 1, water conveying pump 2, one-way control valve 1, water tundish 5, one-way control valve 26, water storage tank 8, aqueous phase stream adjustable valve 9 and the water under meter 10 that connect successively; Described water under meter 10 is connected with described static emulsifying apparatus 24; Described water tundish 5 are communicated with compressed air source by compressed air regulating valve 1, and described water storage tank 8 is communicated with compressed air source by compressed air regulating valve 27;
Described oil phase e Foerderanlage 40 comprises the oil phase preparing tank 11, oil phase transferpump 12, one-way control valve 3 13, oil phase tundish 15, one-way control valve 4 16, oil phase storage tank 18, oil phase flow control valve 19 and the oil phase under meter 20 that connect successively; Described oil phase under meter 20 is connected with described static emulsifying apparatus 24; Described oil phase tundish 15 are communicated with compressed air source by compressed air regulating valve 3 14, and described oil phase storage tank 18 is communicated with compressed air source by compressed air regulating valve 4 17;
Described sensitizer conveying device 50 comprises the sensitizing agent storage tank 21, sensitizing agent transferpump 22 and the sensitizing agent under meter 23 that connect successively; Described sensitizing agent under meter 23 is connected with described static sensitization decollator 25; Described static emulsifying apparatus 24 is connected with described static sensitization decollator 25.Described static sensitization decollator 25 is also connected with filling apparatus 26, can carry out filling to the feed liquid mixing by filling apparatus.The air pressure of described compressed air source is 0.2～1.8 MPa preferably.
Using method of the present utility model is as follows:
(1) closes compression air control valve one, lay down the pressurized air in water tundish, by the water preparing in water preparing tank through water conveying pump and one-way control valve one or utilize potential difference to be delivered to water tundish, in the time that rising to set(ting)value, water material level stops carrying, open compressed air regulating valve one simultaneously, utilize pressurized air to be delivered to water storage tank through one-way control valve two water in water tundish, be incubated for subsequent use.
(2) closes compression air control valve three, lay down the pressurized air in oil phase tundish, by the oil phase preparing in oil phase preparing tank through oil phase transferpump and one-way control valve four or utilize potential difference to be delivered to oil phase tundish, in the time that rising to set(ting)value, oil phase material level stops carrying, open compressed air regulating valve four simultaneously, utilize pressurized air to be delivered to oil phase storage tank through one-way control valve four oil phase in oil phase tundish, be incubated for subsequent use.
(3) open respectively compressed air regulating valve two and compressed air regulating valve four, order open water phase flow rate variable valve and oil phase flow control valve, adopt following control technical, water together enters static emulsifying apparatus in the ratio of setting through oil phase under meter through water under meter, oil phase and forms emulsion matrix under pressurized air effect.Meanwhile, open sensitizing agent transferpump, the sensitizing agent in sensitizing agent storage tank is entered to static sensitization decollator through sensitizing agent under meter in the ratio of setting together with emulsion matrix, complete conveying mixed processes.Mix after sensitization, can, by the feed liquid input filling apparatus mixing, be packaged into powder stick.
In production process, when the material level in water storage tank and oil phase storage tank is during lower than set(ting)value, repeat above-mentioned steps (1) and (2), to supplementary water and oil phase in water storage tank and oil phase storage tank, carry out serialization, automatic production respectively.
The utility model is a kind of anhydrous, oil phase high-pressure delivery pump and matrix transferpump, meet the e Foerderanlage that the emulsion explosive serialization of industry technology developing direction is produced, the aqueous phase solution of this e Foerderanlage, oil-phase solution all adopt pressurized air as transmitting power, thoroughly eradicate the potential safety hazard of high pressure pumping, promote greatly the level of emulsion explosive production line safety in production, and compressed air delivery is impacted little to equipment, the effectively work-ing life of extension device.
The foregoing is only preferred embodiment of the present utility model; not in order to limit the utility model; all within spirit of the present utility model and principle, any amendment of doing, be equal to replacement, improvement etc., within all should being included in protection domain of the present utility model.
Claims (3)
1. the e Foerderanlage for emulsion explosive production mixing of materials, comprise water conveying device (30), oil phase e Foerderanlage (40), sensitizer conveying device (50), static emulsifying apparatus (24) and static sensitization decollator (25), it is characterized in that:
Described water conveying device (30) comprises the water preparing tank (1), water conveying pump (2), one-way control valve one (3), water tundish (5), one-way control valve two (6), water storage tank (8), aqueous phase stream adjustable valve (9) and the water under meter (10) that connect successively; Described water under meter (10) is connected with described static emulsifying apparatus (24); Described water tundish (5) are communicated with compressed air source by compressed air regulating valve one (4), and described water storage tank (8) is communicated with compressed air source by compressed air regulating valve two (7);
Described oil phase e Foerderanlage (40) comprises the oil phase preparing tank (11), oil phase transferpump (12), one-way control valve three (13), oil phase tundish (15), one-way control valve four (16), oil phase storage tank (18), oil phase flow control valve (19) and the oil phase under meter (20) that connect successively; Described oil phase under meter (20) is connected with described static emulsifying apparatus (24); Described oil phase tundish (15) are communicated with compressed air source by compressed air regulating valve three (14), and described oil phase storage tank (18) is communicated with compressed air source by compressed air regulating valve four (17);
Described sensitizer conveying device (50) comprises the sensitizing agent storage tank (21), sensitizing agent transferpump (22) and the sensitizing agent under meter (23) that connect successively; Described sensitizing agent under meter (23) is connected with described static sensitization decollator (25);
Described static emulsifying apparatus (24) is connected with described static sensitization decollator (25).
2. according to claim 1 for the e Foerderanlage of emulsion explosive production mixing of materials, it is characterized in that: described static sensitization decollator (25) connects filling apparatus (26).
According to described in claim 1 or 2 for the e Foerderanlage of emulsion explosive production mixing of materials, it is characterized in that: the air pressure of described compressed air source is 0.2～1.8 MPa.
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201420338952.XU CN203904239U (en) | 2014-06-24 | 2014-06-24 | Conveying device for material mixing in emulsion explosive production |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201420338952.XU CN203904239U (en) | 2014-06-24 | 2014-06-24 | Conveying device for material mixing in emulsion explosive production |
Publications (1)
| Publication Number | Publication Date |
|---|---|
| CN203904239U true CN203904239U (en) | 2014-10-29 |
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| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| CN201420338952.XU Expired - Lifetime CN203904239U (en) | 2014-06-24 | 2014-06-24 | Conveying device for material mixing in emulsion explosive production |
Country Status (1)
| Country | Link |
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| CN (1) | CN203904239U (en) |
Cited By (3)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN104496730A (en) * | 2014-11-27 | 2015-04-08 | 葛洲坝易普力重庆力能民爆股份有限公司 | Pipeline automatic cleaning system and cleaning method |
| CN106946634A (en) * | 2017-03-21 | 2017-07-14 | 浙江利民化工有限公司 | A kind of profit phase gas transporting material device and technique |
| CN106748588B (en) * | 2017-03-03 | 2019-02-26 | 马鞍山江南化工有限责任公司 | Processing unit, processing system and its processing method that waste emulsion explosive recycles |
-
2014
- 2014-06-24 CN CN201420338952.XU patent/CN203904239U/en not_active Expired - Lifetime
Cited By (4)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN104496730A (en) * | 2014-11-27 | 2015-04-08 | 葛洲坝易普力重庆力能民爆股份有限公司 | Pipeline automatic cleaning system and cleaning method |
| CN106748588B (en) * | 2017-03-03 | 2019-02-26 | 马鞍山江南化工有限责任公司 | Processing unit, processing system and its processing method that waste emulsion explosive recycles |
| CN106946634A (en) * | 2017-03-21 | 2017-07-14 | 浙江利民化工有限公司 | A kind of profit phase gas transporting material device and technique |
| CN106946634B (en) * | 2017-03-21 | 2018-11-13 | 浙江利民化工有限公司 | A kind of grease phase gas transporting material device and technique |
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Legal Events
| Date | Code | Title | Description |
|---|---|---|---|
| C14 | Grant of patent or utility model | ||
| GR01 | Patent grant | ||
| CP01 | Change in the name or title of a patent holder | ||
| CP01 | Change in the name or title of a patent holder |
Address after: 655613 Mailu pond 603 mailbox, Fanghua Town, Luliang, Qujing, Yunnan Patentee after: Yunnan Ruida civil explosive Co.,Ltd. Address before: 655613 Mailu pond 603 mailbox, Fanghua Town, Luliang, Qujing, Yunnan Patentee before: STATE NO. 9815 FACTORY |
|
| CX01 | Expiry of patent term | ||
| CX01 | Expiry of patent term |
Granted publication date: 20141029 |