CN201988378U - Synthetic production system for producing semi-finished product - Google Patents
Synthetic production system for producing semi-finished product Download PDFInfo
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- CN201988378U CN201988378U CN2011201116153U CN201120111615U CN201988378U CN 201988378 U CN201988378 U CN 201988378U CN 2011201116153 U CN2011201116153 U CN 2011201116153U CN 201120111615 U CN201120111615 U CN 201120111615U CN 201988378 U CN201988378 U CN 201988378U
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Abstract
The utility model discloses a synthetic production system, in particular to a synthetic production system for producing a semi-finished product, belonging to the technical field of chemical production and providing the synthetic production system for producing the semi-finished product, which is safe and convenient to operate during the adding of a liquid-state chemical raw material into a reaction kettle. The synthetic production system comprises the reaction kettle and a raw material barrel which is positioned outside the reaction kettle and is filled with the liquid-state raw material for production, wherein the upper part of the reaction kettle is provided with a liquid-state raw material feed port; the upper part of the raw material barrel is provided with a liquid-state raw material output port; and a liquid-state raw material extractor is arranged between the liquid-state raw material feed port and the liquid-state raw material output port.
Description
Technical field
The utility model relates to a kind of synthetic production system, especially relates to a kind of half-finished synthetic production system that is used to produce, and belongs to chemical production technical field.
Background technology
Chemical Manufacture generally comprises following process, at first is to generate half-finished industrial chemicals with several single raw materials for production chemical combination in reactor, and then several semi-finished product industrial chemicals are synthesized finished product by chemical combination or composite mode.In half-finished production process, liquid or solid-state raw materials for production to be dropped in the reactor earlier, generate half-finished industrial chemicals by synthetic mode, in this process, raw materials for production generally all adopt the mode of artificial lift to move to add.Because reactor is installed in higher position usually, add the height of reactor self, when adding solid feed, operate also more convenient, labour intensity is not high yet, and when joining liquid raw materials for production in the reactor from Raw material pail, operation is just very inconvenient, concerning operating personnel, not only labour intensity is big, and the security extreme difference, particularly when in reactor, adding, very difficult and dangerous especially as this class corrosivity raw material of sulfuric acid.Simultaneously, omnidistance manually-operated, not only labour intensity is big, and production efficiency is low, the production cost height.
The utility model content
Technical problem to be solved in the utility model is: provide a kind of and can make in reactor handling safety when adding liquid industrial chemicals, be used to produce half-finished synthetic production system easily.
The technical scheme that adopts for solving the problems of the technologies described above is: be used to produce half-finished synthetic production system, comprise reactor and be positioned at the outer Raw material pail that liquid raw materials for production are housed of reactor, be provided with the liquid material input port on the top of reactor, be provided with the liquid material delivery outlet on the top of Raw material pail, between liquid material input port and liquid material delivery outlet, be provided with the liquid material extractor.
Further be, the liquid material extractor is an extraction pump, and extraction pump has an output and an input, and the input of extraction pump is arranged in the bottom of Raw material pail by delivery outlet, and output is communicated with the liquid material input port.
Further be between extracting delivery side of pump and liquid material input port, to be provided with liquid meter.
The optimal way of such scheme is that liquid meter is a zero clearing formula level meter scale.
The beneficial effects of the utility model are: by a liquid material extractor is installed between the delivery outlet of the liquid material input port of reactor and Raw material pail, like this in the time will importing the liquid material in the Raw material pail in the reactor, no matter Raw material pail is positioned at which position of reactor, as long as starting liquid material extractor, just can be very easily with in the liquid raw materials for production input reactor in the Raw material pail, easy to operate, safety, and labour intensity is low.Particularly when adding as this class corrosivity raw material of sulfuric acid in reactor, security more can be guaranteed.
Description of drawings
Fig. 1 is used to produce the structural representation of half-finished synthetic production system for the utility model.
Be labeled as among the figure: reactor 1, Raw material pail 2, input port 3, delivery outlet 4, extraction pump 5, output 51, input 52, liquid meter 6.
The specific embodiment
What be that the utility model provides as shown in Figure 1 a kind ofly can make handling safety when adding liquid industrial chemicals in reactor, is used to produce half-finished synthetic production system easily.Described synthetic production system comprises reactor 1 and the Raw material pail that liquid raw materials for production are housed 2 that is positioned at outside the reactor 1, be provided with liquid material input port 3 on the top of reactor 1, be provided with liquid material delivery outlet 4 on the top of Raw material pail 2, between liquid material input port 3 and liquid material delivery outlet 4, be provided with the liquid material extractor.Like this in will be in the liquid material input reactor 1 time with Raw material pail 2, no matter Raw material pail 2 is positioned at which position of reactor 1, as long as starting liquid material extractor, just can be very easily with in the liquid raw materials for production input reactor 1 in the Raw material pail 2, easy to operate, safety, and labour intensity is low.Particularly when adding as this class corrosivity raw material of sulfuric acid in reactor 1, security more can be guaranteed.
For the structure that makes the input port 3 that cooperates with the liquid material extractor in the above-mentioned embodiment and delivery outlet 4 the simplest, the purchase cost of liquid material extractor is minimum, described liquid material extractor is an extraction pump 5, extraction pump 5 has an output 51 and an input 52, like this, when operation, only the input 52 of extraction pump 5 need be arranged into the bottom of Raw material pail 2 by delivery outlet, output 51 is communicated with liquid material input port 3 and gets final product, do not need to be provided with especially input port 3 and delivery outlet 4, and extraction pump can adopt water-delivery pump commonly used in the present market to get final product, only when adding, just need the water-delivery pump of buying anticorrosion class as this class corrosivity liquid state raw material of sulfuric acid.
In the above-mentioned embodiment, when liquid material being added in the reactor 1, need measure, more convenient in order to make metrological operation, between the output 51 of extraction pump 5 and liquid material input port 3, be provided with liquid meter 6; This liquid meter 6 is zero clearing formula level meter scale.So just the liquid towards raw materials for production do not carry out Weighing before not needing to add, and can measure while adding, and employing zero clearing formula level meter scale, each metering is all started from scratch, the operation of when saving each the metering truth of a matter being write down, metering are also accurate more, operation is also convenient.
Claims (4)
1. be used to produce half-finished synthetic production system, comprise reactor (1) and be positioned at the outer Raw material pail that liquid raw materials for production are housed (2) of reactor (1), be provided with liquid material input port (3) on the top of reactor (1), be provided with liquid material delivery outlet (4) on the top of Raw material pail (2), it is characterized in that: between liquid material input port (3) and liquid material delivery outlet (4), be provided with the liquid material extractor.
2. according to claim 1ly be used to produce half-finished synthetic production system, it is characterized in that: the liquid material extractor is an extraction pump (5), extraction pump (5) has an output (51) and an input (52), the input (52) of extraction pump (5) is arranged in Raw material pail (2) bottom by delivery outlet (4), and output (51) is communicated with liquid material input port (3).
3. according to claim 2ly be used to produce half-finished synthetic production system, it is characterized in that: between the output (51) of extraction pump (5) and liquid material input port (3), be provided with liquid meter (6).
4. according to claim 3ly be used to produce half-finished synthetic production system, it is characterized in that: liquid meter (6) is a zero clearing formula level meter scale.
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN2011201116153U CN201988378U (en) | 2011-04-15 | 2011-04-15 | Synthetic production system for producing semi-finished product |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN2011201116153U CN201988378U (en) | 2011-04-15 | 2011-04-15 | Synthetic production system for producing semi-finished product |
Publications (1)
| Publication Number | Publication Date |
|---|---|
| CN201988378U true CN201988378U (en) | 2011-09-28 |
Family
ID=44664883
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| CN2011201116153U Expired - Fee Related CN201988378U (en) | 2011-04-15 | 2011-04-15 | Synthetic production system for producing semi-finished product |
Country Status (1)
| Country | Link |
|---|---|
| CN (1) | CN201988378U (en) |
Cited By (1)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN103386285A (en) * | 2012-05-11 | 2013-11-13 | 四川汇利实业有限公司 | System for medicine production |
-
2011
- 2011-04-15 CN CN2011201116153U patent/CN201988378U/en not_active Expired - Fee Related
Cited By (1)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN103386285A (en) * | 2012-05-11 | 2013-11-13 | 四川汇利实业有限公司 | System for medicine production |
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Legal Events
| Date | Code | Title | Description |
|---|---|---|---|
| C14 | Grant of patent or utility model | ||
| GR01 | Patent grant | ||
| C17 | Cessation of patent right | ||
| CF01 | Termination of patent right due to non-payment of annual fee |
Granted publication date: 20110928 Termination date: 20140415 |