CN212476582U - Production line of emulsion explosive composite oil phase - Google Patents
Production line of emulsion explosive composite oil phase Download PDFInfo
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- CN212476582U CN212476582U CN202021458704.0U CN202021458704U CN212476582U CN 212476582 U CN212476582 U CN 212476582U CN 202021458704 U CN202021458704 U CN 202021458704U CN 212476582 U CN212476582 U CN 212476582U
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- oleic acid
- condenser
- reation kettle
- storage tank
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Abstract
The utility model discloses a production line of compound oil phase of emulsion explosive, include: the oil-gas preheating device comprises a heat-conducting oil boiler, wherein a sorbic acid storage tank and an oleic acid storage tank are respectively arranged on the right side of the heat-conducting oil boiler, an oleic acid preheating kettle and a first reaction kettle and a second reaction kettle are respectively arranged on the two sides of the oleic acid preheating kettle on the lower portion of the heat-conducting oil boiler, the heat-conducting oil boiler and the oleic acid storage tank are respectively communicated with the oleic acid preheating kettle through connecting pipelines, and the sorbic acid storage tank is respectively connected with the first reaction kettle and the second reaction kettle through two groups of connecting pipes. The utility model discloses continue the reaction in transmitting respectively to first reation kettle and second reation kettle after the completion of oleic acid preheating cauldron raw materials reaction, first reation kettle and second reation kettle react and accomplish the back and carry to condenser department and carry out the condensation, and the condenser is provided with two sets ofly and links to each other with first reation kettle and second reation kettle respectively, has increased its condensation effect, and production line automation degree is high simultaneously, and the production effect obtains effectual promotion.
Description
Technical Field
The utility model relates to a compound oil phase production technical field of emulsion explosive, more specifically are a production line of compound oil phase of emulsion explosive.
Background
Emulsion explosive emulsification extends is to make microdroplets of oxidant salt aqueous solution uniformly dispersed in an oil phase continuous medium containing porous substances such as dispersed bubbles or hollow glass beads and the like by virtue of the action of an emulsifier to form a water-in-oil emulsion explosive, which is a novel industrial explosive developed in the 70 th 20 th century. Emulsion explosives are one type of aqueous explosive. Emulsion explosive is a new product developed in the 70's of the 20 th century. Blabm in the United states in 1969 first described emulsion explosive technology relatively fully, the earliest emulsion explosives being non-detonator sensitive and having to be detonated by means of a relay primer in use. Later, with the research on emulsion explosives, emulsion explosives researched in later period also have detonator sensitivity, good water resistance, good explosion performance, low mechanical sensitivity, good safety and the like, and simultaneously have lower cost than water gel explosives. At present, emulsion explosives are widely used at home and abroad.
The compound oil phase of emulsion explosive is cooled in the production technology of the compound oil phase of the existing emulsion explosive, but the traditional cooling mode easily causes the condition of insufficient cooling effect, and meanwhile, the compound oil phase of the emulsion explosive needs to react with the compound oil phase in the processing process, and various reaction kettles are needed for the reaction of various raw materials, so as to avoid the conflict between the raw materials. Therefore, a new technical solution needs to be provided.
SUMMERY OF THE UTILITY MODEL
An object of the utility model is to provide a production line of compound oil phase of emulsion explosive has solved and has cooled off compound oil phase of emulsion explosive in needs among the prior art's the current production technology of compound oil phase of emulsion explosive, but traditional cooling method causes the not enough condition of cooling effect easily, and compound oil phase of emulsion explosive need react to it in the course of working simultaneously, and the reaction of multiple raw materials need use multiple reation kettle to avoid the problem of conflict between the raw materials.
In order to achieve the above object, the utility model provides a following technical scheme: a production line of an emulsion explosive composite oil phase comprises: the heat conduction oil boiler, the right side of heat conduction oil boiler is equipped with sorbic acid storage tank and oleic acid storage tank respectively, the both sides that the lower part of heat conduction oil boiler was equipped with oleic acid preheating kettle and oleic acid preheating kettle are equipped with first reation kettle and second reation kettle respectively, heat conduction oil boiler and oleic acid storage tank are linked together with oleic acid preheating kettle through connecting tube respectively, sorbic acid storage tank is connected between with first reation kettle and second reation kettle respectively through two sets of connecting pipes, oleic acid preheating kettle is linked together between with first reation kettle and the second reation kettle respectively through connecting tube, the upper portion of second reation kettle is equipped with first condenser and second condenser, the second reation kettle is connected with first condenser through connecting tube, first reation kettle is connected with the second condenser through connecting tube, the right side of first condenser and second condenser is equipped with water cooling tank and first condenser and second condenser pass through connecting tube and water cooling tank Are communicated with each other.
As an optimal implementation mode of the utility model, it is provided with two sets of, two sets of to be equipped with delivery pump and delivery pump between first condenser and second condenser and the water-chilling tank the delivery pump is linked together with two connectors of water-chilling tank respectively.
As an optimal implementation mode of the utility model, the bottom exit that first reation kettle's right side was equipped with sedimentation tank and first reation kettle and second reation kettle communicates with the precipitation tank through connecting tube.
As a preferred embodiment of the present invention, the stirring device is installed at the output end of the first reaction kettle, the second reaction kettle and the oleic acid preheating kettle, which are all provided with the driving motor.
As a preferred embodiment of the present invention, the connecting pipeline of the sorbic acid storage tank, the oleic acid storage tank, the first reaction kettle, the second reaction kettle and the oleic acid preheating kettle is internally provided with a solenoid valve and is connected between the solenoid valve and the external controller.
Compared with the prior art, the beneficial effects of the utility model are as follows:
the utility model discloses set up first reation kettle in the production line, second reation kettle and oleic acid preheating kettle, wherein oleic acid storage tank and conduction oil boiler link to each other with one of them connector of oleic acid preheating kettle, oleic acid preheating kettle links to each other with first reation kettle and second reation kettle through two connecting tubes, sorbic acid storage tank links to each other with first reation kettle and second reation kettle respectively simultaneously, be connected between first reation kettle and the second reation kettle, oleic acid preheating kettle raw materials transmits respectively to continue the reaction in first reation kettle and the second reation kettle after the reaction is accomplished, first reation kettle and second reation kettle carry to condenser department after the reaction is accomplished and condense, the condenser is provided with two sets ofly and links to each other with first reation kettle and second reation kettle respectively, its condensation effect has been increased, the automation degree of while producing is high, the production effect obtains effectual promotion.
Drawings
Fig. 1 is the schematic view of the overall production structure of the present invention.
In the figure, a heat conduction oil boiler-1, a sorbic acid storage tank-2, an oleic acid storage tank-3, a first reaction kettle-4, an oleic acid preheating kettle-5, a second reaction kettle-6, a first condenser-7, a second condenser-8, a delivery pump-9, a precipitation tank-10 and a water cooling tank-11.
Detailed Description
The technical solutions in the embodiments of the present invention will be described clearly and completely with reference to the accompanying drawings in the embodiments of the present invention, and it is obvious that the described embodiments are only some embodiments of the present invention, not all embodiments. Based on the embodiments in the present invention, all other embodiments obtained by a person skilled in the art without creative work belong to the protection scope of the present invention.
Referring to fig. 1, the present invention provides a technical solution: a production line of an emulsion explosive composite oil phase comprises: a heat-conducting oil boiler 1, a sorbic acid storage tank 2 and an oleic acid storage tank 3 are respectively arranged on the right side of the heat-conducting oil boiler 1, an oleic acid preheating kettle 5 is arranged on the lower portion of the heat-conducting oil boiler 1, a first reaction kettle 4 and a second reaction kettle 6 are respectively arranged on two sides of the oleic acid preheating kettle 5, the heat-conducting oil boiler 1 and the oleic acid storage tank 3 are respectively communicated with the oleic acid preheating kettle 5 through connecting pipelines, the sorbic acid storage tank 2 is respectively connected with the first reaction kettle 4 and the second reaction kettle 6 through two groups of connecting pipes, the oleic acid preheating kettle 5 is respectively communicated with the first reaction kettle 4 and the second reaction kettle 6 through connecting pipelines, a first condenser 7 and a second condenser 8 are arranged on the upper portion of the second reaction kettle 6, the second reaction kettle 6 is connected with the first condenser 7 through connecting pipelines, the first reaction kettle 4 is connected with the second condenser 8 through connecting pipelines, the right sides of the first condenser 7 and the second condenser 8 are provided with a water cooling tank 11, the first condenser 7 and the second condenser 8 are communicated with the water cooling tank 11 through connecting pipelines, a first reaction kettle 4, a second reaction kettle 6 and an oleic acid preheating kettle 5 are arranged in a production line, wherein an oleic acid storage tank 3 and a heat conduction oil boiler 1 are connected with one connector of the oleic acid preheating kettle 5, the oleic acid preheating kettle 5 is connected with the first reaction kettle 4 and the second reaction kettle 6 through two connecting pipelines, a sorbic acid storage tank 2 is respectively connected with the first reaction kettle 4 and the second reaction kettle 6, the first reaction kettle 4 and the second reaction kettle 6 are connected, the oleic acid preheating kettle 5 is respectively transferred into the first reaction kettle 4 and the second reaction kettle 6 for continuous reaction after the reaction of the raw materials is finished, the first reaction kettle 4 and the second reaction kettle 6 are transferred to the first condenser 7 and the second condenser 8 for condensation after the reaction is finished, first condenser 7 and second condenser 8 link to each other with first reation kettle and second reation kettle respectively, have increased its condensation effect, and production line automation degree is high simultaneously, and the production effect obtains effectual promotion.
Further improved, as shown in fig. 1: be equipped with between first condenser 7 and second condenser 8 and the water cooling tank 11 delivery pump 9 and be provided with two sets ofly, two sets of delivery pump 9 is linked together with two connectors of water cooling tank 11 respectively, and the raw materials after the condenser cooling will be carried to the setting up of carrying 9 pumps convenience.
Further improved, as shown in fig. 1: the right side of first reation kettle 4 is equipped with the sedimentation tank and the bottom exit of first reation kettle 4 and second reation kettle 6 is linked together through connecting tube and precipitation tank 10, carries the inside residual reactant of first reation kettle 4 and second reation kettle 6 to precipitation tank 10 in the sediment.
Further improved, as shown in fig. 1: first reation kettle 4, second reation kettle 6 and oleic acid preheating cauldron 5's upper portion all is equipped with driving motor and driving motor's output and all installs agitating unit, and the agitating unit of first reation kettle 4, second reation kettle 6 and the inside setting of oleic acid preheating cauldron 5 has increased the reaction effect of its inside raw materials.
Further improved, as shown in fig. 1: the sorbic acid storage tank 2, the oleic acid storage tank 3, the first reaction kettle 4, the second reaction kettle 6 and the oleic acid preheating kettle 5 are respectively provided with an electromagnetic valve inside the connecting pipeline, the electromagnetic valves are connected with an external controller, and the arrangement of the electromagnetic valves increases the convenience of conveying raw materials of a production line and facilitates control.
The utility model is provided with a first reaction kettle 4, a second reaction kettle 6 and an oleic acid preheating kettle 5 in the production line, wherein an oleic acid storage tank 3 and a heat transfer oil boiler 1 are connected with one of connectors of the oleic acid preheating kettle 5, the oleic acid preheating kettle 5 is connected with the first reaction kettle 4 and the second reaction kettle 6 through two connecting pipelines, a sorbic acid storage tank 2 is respectively connected with the first reaction kettle 4 and the second reaction kettle 6, the first reaction kettle 4 is connected with the second reaction kettle 6, the oleic acid preheating kettle 5 is respectively transmitted into the first reaction kettle 4 and the second reaction kettle 6 for continuous reaction after the raw material reaction is finished, the first reaction kettle 4 and the second reaction kettle 6 are respectively transmitted to a first condenser 7 and a second condenser 8 for condensation after the reaction is finished, the first condenser 7 and the second condenser 8 are respectively connected with the first reaction kettle and the second reaction kettle, the condensation effect is increased, meanwhile, the automation degree of the production line is high, and the production effect is effectively improved.
Finally, it should be noted that: although the present invention has been described in detail with reference to the foregoing embodiments, it will be apparent to those skilled in the art that modifications may be made to the embodiments described in the foregoing embodiments, or equivalents may be substituted for elements thereof. Any modification, equivalent replacement, or improvement made within the spirit and principle of the present invention should be included in the protection scope of the present invention.
Claims (5)
1. The production line of the compound oil phase of the emulsion explosive is characterized in that: the method comprises the following steps: the heat conduction oil boiler, the right side of heat conduction oil boiler is equipped with sorbic acid storage tank and oleic acid storage tank respectively, the both sides that the lower part of heat conduction oil boiler was equipped with oleic acid preheating kettle and oleic acid preheating kettle are equipped with first reation kettle and second reation kettle respectively, heat conduction oil boiler and oleic acid storage tank are linked together with oleic acid preheating kettle through connecting tube respectively, sorbic acid storage tank is connected between with first reation kettle and second reation kettle respectively through two sets of connecting pipes, oleic acid preheating kettle is linked together between with first reation kettle and the second reation kettle respectively through connecting tube, the upper portion of second reation kettle is equipped with first condenser and second condenser, the second reation kettle is connected with first condenser through connecting tube, first reation kettle is connected with the second condenser through connecting tube, the right side of first condenser and second condenser is equipped with water cooling tank and first condenser and second condenser pass through connecting tube and water cooling tank Are communicated with each other.
2. The production line of the composite oil phase of the emulsion explosive according to claim 1, which is characterized in that: and two groups of delivery pumps are arranged between the first condenser, the second condenser and the water cooling tank and are respectively communicated with two connectors of the water cooling tank.
3. The production line of the composite oil phase of the emulsion explosive according to claim 1, which is characterized in that: the right side of the first reaction kettle is provided with a sedimentation tank, and the bottom outlets of the first reaction kettle and the second reaction kettle are communicated with the sedimentation tank through a connecting pipeline.
4. The production line of the composite oil phase of the emulsion explosive according to claim 3, characterized in that: the upper parts of the first reaction kettle, the second reaction kettle and the oleic acid preheating kettle are all provided with driving motors, and the output ends of the driving motors are all provided with stirring devices.
5. The production line of the composite oil phase of the emulsion explosive according to claim 4, characterized in that: the interior of the connecting pipeline of the sorbic acid storage tank, the oleic acid storage tank, the first reaction kettle, the second reaction kettle and the oleic acid preheating kettle is provided with an electromagnetic valve, and the electromagnetic valve is connected with an external controller.
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN202021458704.0U CN212476582U (en) | 2020-07-22 | 2020-07-22 | Production line of emulsion explosive composite oil phase |
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| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN202021458704.0U CN212476582U (en) | 2020-07-22 | 2020-07-22 | Production line of emulsion explosive composite oil phase |
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| CN212476582U true CN212476582U (en) | 2021-02-05 |
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| CN202021458704.0U Expired - Fee Related CN212476582U (en) | 2020-07-22 | 2020-07-22 | Production line of emulsion explosive composite oil phase |
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Cited By (1)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN112028720A (en) * | 2020-07-22 | 2020-12-04 | 安徽省百舸实业有限公司 | Production line and production method of emulsion explosive composite oil phase |
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2020
- 2020-07-22 CN CN202021458704.0U patent/CN212476582U/en not_active Expired - Fee Related
Cited By (1)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN112028720A (en) * | 2020-07-22 | 2020-12-04 | 安徽省百舸实业有限公司 | Production line and production method of emulsion explosive composite oil phase |
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| CF01 | Termination of patent right due to non-payment of annual fee |
Granted publication date: 20210205 Termination date: 20210722 |
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| CF01 | Termination of patent right due to non-payment of annual fee |