CN216584810U - Liquid integrated oil phase system for emulsion explosive production - Google Patents
Liquid integrated oil phase system for emulsion explosive production Download PDFInfo
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- CN216584810U CN216584810U CN202123368993.2U CN202123368993U CN216584810U CN 216584810 U CN216584810 U CN 216584810U CN 202123368993 U CN202123368993 U CN 202123368993U CN 216584810 U CN216584810 U CN 216584810U
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Abstract
The utility model discloses a liquid state integration oil phase system for emulsion explosive production, including oil phase storage device and steam generator, be connected with the inlet pipe on the feed inlet of oil phase storage device, be provided with the unloading pump on the inlet pipe, the discharge gate of oil phase storage device is connected to the oil phase storage tank between the oil phase preparation through the discharging pipe, is provided with baiting valve and blowing pump on the discharging pipe; the oil phase storage device comprises a storage tank body, wherein a stirring mechanism is fixed at the top of the storage tank body through a rack, a solid ammonium nitrate feed port and a liquid oil phase feed port are further formed in the top of the storage tank body on the periphery side of the stirring mechanism, a steam coil pipe is arranged in the storage tank body on the periphery side of the stirring mechanism, and two ends of the steam coil pipe are connected with the steam generating device. Raw material storehouses are not required to be configured, packaging is not required, the environmental protection problem caused by pollution is avoided, the production beat is accelerated, and the production efficiency is improved.
Description
Technical Field
The utility model relates to emulsion explosive production technical field, concretely relates to liquid state integration oil phase system for emulsion explosive production.
Background
In the production process of the emulsion explosive, a composite oil phase raw material needs to be added, the currently used composite oil phase product is completely packaged in a 'carton + plastic inner bag' mode, and is stored in a storehouse in a solid state form after being cooled and solidified.
However, the above method has many disadvantages, specifically: firstly, a raw material warehouse is specially configured for storing raw materials, so that the resource use is unreasonable, and in the production process, the raw materials need to be transported from the warehouse to a production site, so that time and labor are wasted; secondly, the price of the carton rises, the packaging cost of the oil phase product is greatly increased, and the purchase cost rises; thirdly, the oil phase is adhered to the inner bag after being solidified, so that material waste is caused, the inner bag adhered with the oil phase also becomes a pollution source, and the oil phase is not easy to treat, so that the problem of environmental protection is caused.
Disclosure of Invention
The not enough to prior art, the utility model aims at providing a liquid integrative oil phase system for emulsion explosive production, keep warm to liquid oil phase through steam heating and store, can deliver to the production site with liquid oil phase at any time.
In order to achieve the above purpose, the utility model adopts the following technical scheme:
a liquid state integration oil phase system for emulsion explosive production, its key lies in: the oil phase preparation system comprises an oil phase storage device and a steam generation device, wherein a feed pipe is connected to a feed inlet of the oil phase storage device, a discharge pump is arranged on the feed pipe, a discharge outlet of the oil phase storage device is connected to an oil phase storage tank of an oil phase preparation room through a discharge pipe, and a discharge valve and a discharge pump are arranged on the discharge pipe;
the oil phase storage device comprises a storage tank body, wherein a stirring mechanism is fixed at the top of the storage tank body through a rack, a stirring shaft of the stirring mechanism stretches into the storage tank body, a plurality of stirring paddles are arranged on the stirring shaft, a solid ammonium nitrate feed port and a liquid oil phase feed port are further arranged at the top of the storage tank body on the periphery side of the stirring mechanism, a steam coil pipe is arranged in the storage tank body on the periphery side of the stirring mechanism, the two ends of the steam coil pipe are connected with an air inlet and an air outlet of the steam generating device, the distance between the steam coil pipe and the bottom of the storage tank body is not more than 10mm, a discharge port and a drain outlet are arranged at the bottom of the storage tank body, the discharge port is connected with the discharge pipe, and a drain pipe is connected on the drain outlet.
Further, the storage tank body is composed of an inner wall made of carbon steel, an outer wall made of stainless steel and a heat insulation material filled between the inner wall and the outer wall.
Further, reserve mouth and breathe the mouth still seted up at the top of holding vessel body, reserve the flange that is equipped with the blind lid on the mouth, breathe and be equipped with the breather valve on the mouth.
Furthermore, the bottom of the storage tank body is provided with a liquid level port, a first temperature measuring port and a second temperature measuring port.
Furthermore, the height of the inlet end of the sewage draining outlet is lower than the inner bottom surface of the storage tank body.
Further, a guardrail with the height not less than 1200mm is arranged at the top of the storage tank body.
The utility model discloses a show the effect and be: simple structure, high durability and convenient use, liquid integrative oil phase passes through tank car and transports to the factory in, squeeze into oil phase storage device with the pump of unloading with liquid oil phase through the inlet pipe and save, oil phase storage device's storage tank is furnished with agitating unit, and adopted steam heating to keep warm the storage tank, open the baiting valve of oil phase storage tank during the plant operation, supply the plant operation to use in the oil phase storage tank between water oil phase preparation through the blowing pump sending, compare in the conventional art, need not dispose raw and other materials storehouse, need not pack, and can not cause the pollution to cause the environmental protection problem, can carry the liquid oil phase in the storage tank to the production site at any time, the time of raw materials preparation has been reduced, the production beat has been accelerated, help improving production efficiency.
Drawings
Fig. 1 is a schematic view of the pipeline structure of the present invention;
FIG. 2 is a schematic structural view of the oil phase storage device;
FIG. 3 is an enlarged partial schematic view of A in FIG. 2;
FIG. 4 is a schematic view showing the position of the nozzle of the oil phase storage device
Detailed Description
The following provides a more detailed description of the embodiments and the operation of the present invention with reference to the accompanying drawings.
As shown in fig. 1, a liquid integration oil phase system for emulsion explosive production, includes oil phase storage device 1 and steam generation device 2, be connected with inlet pipe 3 on oil phase storage device 1's the feed inlet, be provided with discharge pump 4 on the inlet pipe 3, oil phase storage device 1's discharge gate is connected to the oil phase storage tank between the oil phase preparation through discharging pipe 5 be provided with baiting valve 6 and blowing pump 7 on discharging pipe 5.
Referring to fig. 2-4, the oil phase storage device 1 includes a storage tank 11, a stirring mechanism 13 is fixed on the top of the storage tank 11 through a frame 12, a stirring shaft 14 of the stirring mechanism 13 extends into the storage tank 11, a plurality of stirring paddles 15 are arranged on the stirring shaft 14, a guardrail 16 with a height of not less than 1200mm is arranged on the top of the storage tank 11, a square manhole 119, a solid ammonium nitrate feed port 17 and a liquid oil phase feed port 18 are further arranged on the top of the storage tank 11 around the stirring mechanism 13, the liquid oil phase feed port 18 is connected with the feed pipe 3, a reserved port 19 and a breathing port 110 are further arranged on the top of the storage tank 11, a connecting flange with a blind cover is arranged on the reserved port 19, a breathing valve is arranged on the breathing port 110 to discharge excessive air pressure, and a steam coil pipe 111 is arranged in the storage tank 11 around the stirring mechanism 13, this steam coil 111 both ends with steam generator 2's air inlet, gas vent link to each other, just steam coil 111 is not more than 10mm apart from the distance of the 11 bottoms of the holding vessel body, the bottom of the holding vessel body 11 is provided with discharge gate 112 and drain 113, discharge gate 112 with discharging pipe 5 links to each other, be connected with blow off pipe 114 on the drain 113, the entrance point height of drain 113 is less than the interior bottom surface of the holding vessel body 11, the bottom of the holding vessel body 11 is provided with the liquid level mouth 115 that is used for detecting the inside liquid level of the holding vessel body 11, is used for carrying out temperature measuring's first temperature measurement mouth 116 and second temperature measurement mouth 117 and the sample connection 118 that is used for the liquid oil phase of sample to the inside liquid oil phase of the holding vessel body 11.
In this example, the storage tank 11 is composed of an inner wall made of carbon steel, an outer wall made of stainless steel, and a heat insulating material filled between the inner wall and the outer wall, wherein the inner wall is made of Q235 carbon steel, the outer wall is made of 304 stainless steel, and the heat insulating material is made of aluminum silicate.
The liquid integrated oil phase is transported to a factory through a tank car, the liquid oil phase is pumped into an oil phase storage device 1 through a feeding pipe 3 by a discharging pump 4 to be stored, a storage tank body 11 of the oil phase storage device 1 is provided with a stirring mechanism 13, a steam generating device 2 is adopted to carry out steam heating and heat preservation on the storage tank body 11, the steam temperature control range is 85-95 ℃, the material temperature control range in the storage tank body 11 is 70-80 ℃, a discharging valve 6 of the oil phase storage device 1 is opened during production and use, and the liquid oil phase is pumped into an oil phase storage tank between water and oil phase preparation by a discharging pump 7 to be used for production.
The technical scheme provided by the utility model is introduced in detail above. The principles and embodiments of the present invention have been explained herein using specific examples, and the above descriptions of the embodiments are only used to help understand the method and its core ideas of the present invention. It should be noted that, for those skilled in the art, without departing from the principle of the present invention, the present invention can be further modified and modified, and such modifications and modifications also fall within the protection scope of the appended claims.
Claims (6)
1. A liquid state integrated oil phase system for emulsion explosive production which characterized in that: the oil phase preparation system comprises an oil phase storage device and a steam generation device, wherein a feed pipe is connected to a feed inlet of the oil phase storage device, a discharge pump is arranged on the feed pipe, a discharge outlet of the oil phase storage device is connected to an oil phase storage tank of an oil phase preparation room through a discharge pipe, and a discharge valve and a discharge pump are arranged on the discharge pipe;
the oil phase storage device comprises a storage tank body, wherein a stirring mechanism is fixed at the top of the storage tank body through a rack, a stirring shaft of the stirring mechanism stretches into the storage tank body, a plurality of stirring paddles are arranged on the stirring shaft, a solid ammonium nitrate feed port and a liquid oil phase feed port are further arranged at the top of the storage tank body on the periphery side of the stirring mechanism, a steam coil pipe is arranged in the storage tank body on the periphery side of the stirring mechanism, the two ends of the steam coil pipe are connected with an air inlet and an air outlet of the steam generating device, the distance between the steam coil pipe and the bottom of the storage tank body is not more than 10mm, a discharge port and a drain outlet are arranged at the bottom of the storage tank body, the discharge port is connected with the discharge pipe, and a drain pipe is connected on the drain outlet.
2. The liquid integrated oil phase system for emulsion explosive production according to claim 1, wherein: the storage tank body is composed of an inner wall made of carbon steel, an outer wall made of stainless steel and a heat insulation material filled between the inner wall and the outer wall.
3. The liquid integrated oil phase system for emulsion explosive production according to claim 1, wherein: reserve mouth and breathe the mouth still has been seted up at the top of holding vessel body, reserve the flange that is equipped with the blind lid on the mouth, breathe and be equipped with the breather valve on the mouth.
4. The liquid integrated oil phase system for emulsion explosive production according to claim 1, wherein: the bottom of the storage tank body is provided with a liquid level port, a first temperature measuring port and a second temperature measuring port.
5. The liquid integrated oil phase system for emulsion explosive production according to claim 1, wherein: the inlet end of the sewage draining outlet is lower than the inner bottom surface of the storage tank body.
6. The liquid integrated oil phase system for emulsion explosive production according to claim 1, wherein: the top of the storage tank body is provided with a guardrail with the height not less than 1200 mm.
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN202123368993.2U CN216584810U (en) | 2021-12-29 | 2021-12-29 | Liquid integrated oil phase system for emulsion explosive production |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN202123368993.2U CN216584810U (en) | 2021-12-29 | 2021-12-29 | Liquid integrated oil phase system for emulsion explosive production |
Publications (1)
| Publication Number | Publication Date |
|---|---|
| CN216584810U true CN216584810U (en) | 2022-05-24 |
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Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| CN202123368993.2U Active CN216584810U (en) | 2021-12-29 | 2021-12-29 | Liquid integrated oil phase system for emulsion explosive production |
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| Country | Link |
|---|---|
| CN (1) | CN216584810U (en) |
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2021
- 2021-12-29 CN CN202123368993.2U patent/CN216584810U/en active Active
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