CN106316723A - Composite oil phase preparation discharge system - Google Patents
Composite oil phase preparation discharge system Download PDFInfo
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- CN106316723A CN106316723A CN201510385229.6A CN201510385229A CN106316723A CN 106316723 A CN106316723 A CN 106316723A CN 201510385229 A CN201510385229 A CN 201510385229A CN 106316723 A CN106316723 A CN 106316723A
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Abstract
The invention discloses a composite oil phase preparation discharge system. A preparation tank and a storage tank are connected through a valve 3 and a pipeline; the preparation tank is connected to a heating container through a pipeline, wherein a flowmeter 1 and a valve 1 are on the pipeline; the preparation tank is connected to a single body oil phase chamber through a pipeline, wherein a flowmeter 2 and a valve 2 are on the pipeline; the preparation tank is connected to a steam chamber through a pipeline, wherein a steam valve is on the pipeline; a weight sensor 1 and a weight sensor 2 are respectively arranged on the bottoms of the preparation tank and the storage tank. According to the physical characteristics of a single body oil phase, the single body oil phase is heated until molten into liquid; the liquid is delivered into the preparation tank through the flowmeter, the valve and the pipeline; another single body oil phase is directly delivered to the preparation tank through the flowmeter and the valve; automatic heating, stirring and mixing are conducted in the preparation tank; the mixture is delivered to a production storage tank through the valve 3. All the parts in the system are controlled by PLC, such that the composite oil proportioning is accurate. Unstable human factors are overcome; fixed number of production staffs on site is reduced; the automation degree is high; cost is reduced; and production quality is improved.
Description
Technical field
The present invention relates to the composite oil phase preparation material drain system during expanded ammonium nitrate explosive produces.
Background technology
Composite oil phase during expanded ammonium nitrate explosive produces at present is all artificial preparation, artificial blowing, has the disadvantages that (1) automaticity is low;(2) production staffing is increased;(3) to affect composite oil phase proportioning inaccurate in anthropic factor, thus affects product quality.
Summary of the invention
The present invention, in order to improve expanded ammonium nitrate explosive production line automation level, makes composite oil phase proportion speed, the special composite oil phase that proposes prepare material drain system.
The technical scheme is that for this, composite oil phase preparation material drain system, including preparing tank and holding vessel, preparing tank and holding vessel are connected by valve three and pipeline, it is characterized in that: being connected by pipeline on preparing tank has effusion meter one, valve one to adding heat container, connecting also by pipeline and have effusion meter two, valve two to monomer oil phase room, connecting also by pipeline has steam valve to vaporium;Weight sensor one and weight sensor two it is additionally provided with bottom preparing tank and holding vessel.
Further it is improved by: be also respectively provided with blender one and blender two in preparing tank and holding vessel, and on the sidewall of preparing tank and holding vessel, be provided with temperature sensor one and temperature sensor two respectively.
Further it is improved by: described add heat container, effusion meter one, valve one, effusion meter two, valve two, weight sensor one, weight sensor two, blender one, blender two, temperature sensor one, temperature sensor two are connected to PLC.
Beneficial effect:
The present invention, according to the physical characteristic of monomer oil phase, is heated to dissolve and is changed into liquid, by effusion meter one, valve one, makes to be piped to preparing tank, and another kind of monomer oil phase is directly delivered to preparing tank by effusion meter two, valve two;The automatic heated and stirred of preparing tank is delivered to produce storage tank by pneumatic operated valve after merging.In system, effusion meter one, valve one, effusion meter two, valve two, weight sensor one, weight sensor two, blender one, blender two, temperature sensor one, temperature sensor two are connected to PLC.
The composite oil phase of the present invention realizes automatically preparing blowing, with temperature, weight, flow as foundation, control the preparation automatically of several monomer oil phase by PLC, preparing tank automatic stirring merges and the blowing of valve, make composite oil phase proportion speed, overcome the instability of anthropic factor, decrease produced on-site staffing simultaneously.Automaticity is high, reduces cost, improves the quality of production.
Accompanying drawing explanation
Fig. 1 is the connection diagram of the present invention.
In figure, 1 is to add heat container, and 2 is valve one, and 3 is effusion meter one, 4-1 is blender one, and 4-2 is blender two, and 5 is effusion meter two, 6 is valve two, and 7-1 is temperature sensor one, and 7-2 is temperature sensor two, 8 is LOAD CELLS one, and 9 is valve three, and 10 is steam valve, 11 is LOAD CELLS two, and 12 is preparing tank, and 13 is holding vessel, 14 is monomer oil phase case, and 15 is vaporium, and 16 is PLC.
Detailed description of the invention
The present invention is as shown in Figure 1.
Composite oil phase preparation material drain system, including preparing tank 12 and holding vessel 13, preparing tank 12 and holding vessel 13 are connected by valve 39 and pipeline, connected by pipeline on preparing tank 12 and have effusion meter 1, valve 1 to adding heat container 1, connecting also by pipeline and have effusion meter 25, valve 26 to monomer oil phase room 14, connecting also by pipeline has steam valve 10 to vaporium 15;Weight sensor 1 and weight sensor 2 11 it is additionally provided with bottom preparing tank 12 and holding vessel 13.
It is also respectively provided with blender one 4-1 and blender two 4-2 in preparing tank 12 and holding vessel 13, and on the sidewall of preparing tank 12 and holding vessel 13, is provided with temperature sensor one 7-1 and temperature sensor two 7-2 respectively.
Add heat container 1, effusion meter 1, valve 1, effusion meter 25, valve 26, weight sensor 1, weight sensor 2 11, blender one 4-1, blender two 4-2, temperature sensor one 7-1, temperature sensor two 7-2 are connected to PLC 16.
Using method:
Physical characteristic according to monomer oil phase, heat to dissolve by it in adding heat container 1 and be changed into liquid, PLC 16 collects the signal of LOAD CELLS 1 conveying of preparing tank 12, and calculate two kinds of monomer oil phase additions according to proportioning, monomer oil phase discharges rear PLC 16 will instruct steam valve 10 and blender 4-1 startup, when in preparing tank 12, temperature reaches composite oil phase complete Fusion Strain, temperature sensor one 7-1 will be to a signal to PLC 16, and PLC 16 then instructs steam valve 10 and blender one 4-1 closes.
Now composite oil phase has been prepared, PLC 16 instructs preparing tank 12 valve 39 and opens, blowing is started toward holding vessel 13, when holding vessel 13 is piled, weight sensor 2 11 will be to a signal to PLC 16, and PLC 16 then instructs valve 39 and closes, holding vessel 13 temperature is controlled to be maintained at certain limit by PLC 16, being beneficial to produce needs, so far, a composite oil phase automatically makes blowing process and i.e. completes.
Claims (3)
1. composite oil phase preparation material drain system, including preparing tank and holding vessel, preparing tank and holding vessel are connected by valve three and pipeline, it is characterized in that: being connected by pipeline on preparing tank has effusion meter one, valve one to adding heat container, connecting also by pipeline and have effusion meter two, valve two to monomer oil phase room, connecting also by pipeline has steam valve to vaporium;Weight sensor one and weight sensor two it is additionally provided with bottom preparing tank and holding vessel.
Composite oil phase the most according to claim 1 preparation material drain system, it is characterized in that: be also respectively provided with blender one and blender two in preparing tank and holding vessel, and on the sidewall of preparing tank and holding vessel, be provided with temperature sensor one and temperature sensor two respectively.
Composite oil phase the most according to claim 1 and 2 preparation material drain system, it is characterised in that: described add heat container, effusion meter one, valve one, effusion meter two, valve two, weight sensor one, weight sensor two, blender one, blender two, temperature sensor one, temperature sensor two are connected to PLC.
Priority Applications (1)
Application Number | Priority Date | Filing Date | Title |
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CN201510385229.6A CN106316723A (en) | 2015-07-06 | 2015-07-06 | Composite oil phase preparation discharge system |
Applications Claiming Priority (1)
Application Number | Priority Date | Filing Date | Title |
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CN201510385229.6A CN106316723A (en) | 2015-07-06 | 2015-07-06 | Composite oil phase preparation discharge system |
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CN106316723A true CN106316723A (en) | 2017-01-11 |
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CN201510385229.6A Pending CN106316723A (en) | 2015-07-06 | 2015-07-06 | Composite oil phase preparation discharge system |
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Cited By (1)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
CN106813762A (en) * | 2017-03-29 | 2017-06-09 | 广东宏大罗化民爆有限公司 | A kind of device that can accurately read composite oil phase weight |
-
2015
- 2015-07-06 CN CN201510385229.6A patent/CN106316723A/en active Pending
Cited By (1)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
CN106813762A (en) * | 2017-03-29 | 2017-06-09 | 广东宏大罗化民爆有限公司 | A kind of device that can accurately read composite oil phase weight |
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Application publication date: 20170111 |