CN203916658U - Chemical industry still mixing device - Google Patents
Chemical industry still mixing device Download PDFInfo
- Publication number
- CN203916658U CN203916658U CN201420290256.6U CN201420290256U CN203916658U CN 203916658 U CN203916658 U CN 203916658U CN 201420290256 U CN201420290256 U CN 201420290256U CN 203916658 U CN203916658 U CN 203916658U
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- China
- Prior art keywords
- pipeline
- deionized water
- water pipeline
- valve
- hot deionized
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Abstract
The utility model relates to polyvinyl-chloride use kettle technical field, is a kind of chemical industry still mixing device; It comprises kettle, monomer line, terminator pipeline, hot deionized water pipeline, initator pipeline, cold deionized water pipeline, dispersant pipeline and buffer pipeline; In the upper end of kettle, be installed with respectively monomer line and terminator pipeline, on monomer line and terminator pipeline, be installed with valve, in the bottom of kettle, there are discharge end and feed end, on discharge end, be installed with valve, on feed end, be installed with hot deionized water pipeline, on hot deionized water pipeline, be installed with respectively master control valve and heat without ion valve, at master control valve and heat, be installed with the mixing tank communicating with hot deionized water pipeline on without the hot deionized water pipeline between ion valve.The utility model is rational in infrastructure, easy to use, by mixing tank is set, can effectively make each material fully mix in mixing tank, thereby improve product quality.
Description
Technical field
The utility model relates to polyvinyl-chloride use kettle technical field, is a kind of chemical industry still mixing device.
Background technology
At present, when carrying out Production of PVC, general cold deionized water, the hot deionized water intersection enter material way of adopting, but because the pipeline on reactor is many, valve is many, therefore each material is prone to inhomogeneous phenomenon when mixing, and causes product quality to be difficult for the problem guaranteeing like this with regard to existing because charging is inhomogeneous.
Summary of the invention
The utility model provides a kind of chemical industry still mixing device, has overcome the deficiency of above-mentioned prior art, and it can effectively solve and because charging is inhomogeneous, cause product quality to be difficult for the problem guaranteeing.
The technical solution of the utility model is achieved like this: a kind of chemical industry still mixing device, comprises kettle, monomer line, terminator pipeline, hot deionized water pipeline, initator pipeline, cold deionized water pipeline, dispersant pipeline and buffer pipeline, in the upper end of kettle, be installed with respectively monomer line and terminator pipeline, on monomer line and terminator pipeline, be installed with valve, in the bottom of kettle, there are discharge end and feed end, on discharge end, be installed with valve, on feed end, be installed with hot deionized water pipeline, on hot deionized water pipeline, be installed with respectively master control valve and heat without ion valve, at master control valve and heat, be installed with the mixing tank communicating with hot deionized water pipeline on without the hot deionized water pipeline between ion valve, at mixing tank, be parallel with respectively the initator pipeline communicating with hot deionized water pipeline with heat on without the hot deionized water pipeline between ion valve, dispersant pipeline, buffer pipeline and cold deionized water pipeline, at initator pipeline, dispersant pipeline, on buffer pipeline and cold deionized water pipeline, be installed with respectively valve, in monomer line, terminator pipeline, initator pipeline, dispersant pipeline, buffer pipeline, on hot deionized water pipeline and cold deionized water pipeline, be installed with respectively mass flowmenter, agitator is installed in kettle.
As preferably, above-mentioned mixing tank comprises tank body, upper spacer and lower clapboard, in tank body, from right-to-left, be intervally distributed with tank body top and have the lower clapboard of spacing and have the upper spacer of spacing with tank base, in lower end, tank body right side, there is charging aperture, in upper end, tank body left side, have discharging opening, the charging aperture of described tank body and discharging opening are fixedly installed togather with hot deionized water pipeline respectively.
As preferably, the hinged baffle plate that is left low right high shape that is provided with in the left side of above-mentioned upper spacer, the left end height of described baffle plate is lower than the height of discharging opening.
As preferably, above-mentioned autoclave body bottom is installed with agitator, and the stirring end of described agitator is positioned at kettle.
The utility model is rational in infrastructure, easy to use, by mixing tank is set, can effectively make each material fully mix in mixing tank, thereby improve product quality.
Accompanying drawing explanation
Fig. 1 is process flow diagram of the present utility model.
Fig. 2 is that the master of mixing tank in Fig. 1 looks perspective view.
Coding in figure is respectively: 1 is kettle, and 2 is monomer line, and 3 is terminator pipeline, and 4 is hot deionized water pipeline, 5 is initator pipeline, and 6 is cold deionized water pipeline, and 7 is dispersant pipeline, 8 is buffer pipeline, and 9 is discharge end, and 10 is feed end, 11 is valve, and 12 is master control valve, and 13 is that heat is without ion valve, 14 is mixing tank, and 15 is tank body, and 16 is upper spacer, 17 is lower clapboard, and 18 is baffle plate, and 19 is agitator.
The specific embodiment
As shown in Figure 1, this chemical industry still mixing device, comprises kettle 1, monomer line 2, terminator pipeline 3, hot deionized water pipeline 4, initator pipeline 5, cold deionized water pipeline 6, dispersant pipeline 7 and buffer pipeline 8, in the upper end of kettle 1, be installed with respectively monomer line 2 and terminator pipeline 3, on monomer line 2 and terminator pipeline 3, be installed with valve 11, in the bottom of kettle 1, there are discharge end 9 and feed end 10, on discharge end 9, be installed with valve 11, on feed end 10, be installed with hot deionized water pipeline 4, on hot deionized water pipeline 4, be installed with respectively master control valve 12 and heat without ion valve 13, at master control valve 12 and heat, be installed with the mixing tank 14 communicating with hot deionized water pipeline 4 on without the hot deionized water pipeline 4 between ion valve 13, at mixing tank 14, be parallel with respectively the initator pipeline 5 communicating with hot deionized water pipeline 4 with heat on without the hot deionized water pipeline 4 between ion valve 13, dispersant pipeline 7, buffer pipeline 8 and cold deionized water pipeline 6, at initator pipeline 5, dispersant pipeline 7, on buffer pipeline 8 and cold deionized water pipeline 6, be installed with respectively valve 11, in monomer line 2, terminator pipeline 3, initator pipeline 5, dispersant pipeline 7, buffer pipeline 8, on hot deionized water pipeline 4 and cold deionized water pipeline 6, be installed with respectively mass flowmenter, agitator 19 is installed in kettle 1.By mixing tank 14 is set, by various valves 11 and the hot regulation and control without ion valve 13, can effectively make each material in the interior abundant mixing of mixing tank 14, thereby improve product quality.Mixing tank 14 can adopt existing known technology.
As shown in Figure 2, described mixing tank 14 comprises tank body 15, upper spacer 16 and lower clapboard 17, in tank body 15, from right-to-left, be intervally distributed with tank body 15 tops and have the lower clapboard 17 of spacing and have the upper spacer 16 of spacing with tank body 15 bottoms, in tank body 15 lower ends, right side, there is charging aperture, in tank body 15 upper ends, left side, there is discharging opening, the charging aperture of tank body 15 and discharging opening are fixedly installed togather with hot deionized water pipeline 4 respectively, and such mixing tank 14 can effectively mix each material.
As shown in Figure 2, the hinged baffle plate 18 that is left low right high shape that is provided with in the left side of described upper spacer 16, the left end height of baffle plate 18, lower than the height of discharging opening, like this, by the barrier effect of baffle plate 18, has improved mixing efficiency thereby can extend incorporation time.
As shown in Figure 1, for the ease of stirring, kettle 1 bottom is installed with agitator 19, and the stirring end of agitator 19 is positioned at kettle 1.
Claims (4)
1. a chemical industry still mixing device, it is characterized in that, comprise kettle (1), monomer line (2), terminator pipeline (3), hot deionized water pipeline (4), initator pipeline (5), cold deionized water pipeline (6), dispersant pipeline (7) and buffer pipeline (8), in the upper end of kettle (1), be installed with respectively monomer line (2) and terminator pipeline (3), on monomer line (2) and terminator pipeline (3), be installed with valve (11), in the bottom of kettle (1), there are discharge end (9) and feed end (10), on discharge end (9), be installed with valve (11), on feed end (10), be installed with hot deionized water pipeline (4), on hot deionized water pipeline (4), be installed with respectively master control valve (12) and heat without ion valve (13), at master control valve (12) and heat, be installed with the mixing tank (14) communicating with hot deionized water pipeline (4) on without the hot deionized water pipeline (4) between ion valve (13), at mixing tank (14), be parallel with respectively the initator pipeline (5) communicating with hot deionized water pipeline (4) with heat on without the hot deionized water pipeline (4) between ion valve (13), dispersant pipeline (7), buffer pipeline (8) and cold deionized water pipeline (6), in initator pipeline (5), dispersant pipeline (7), on buffer pipeline (8) and cold deionized water pipeline (6), be installed with respectively valve (11), in monomer line (2), terminator pipeline (3), initator pipeline (5), dispersant pipeline (7), buffer pipeline (8), on hot deionized water pipeline (4) and cold deionized water pipeline (6), be installed with respectively mass flowmenter, agitator (19) is installed in kettle (1).
2. chemical industry still mixing device according to claim 1, it is characterized in that, described mixing tank (14) comprises tank body (15), upper spacer (16) and lower clapboard (17), in tank body (15), from right-to-left, be intervally distributed with tank body (15) top and have the lower clapboard (17) of spacing and have the upper spacer (16) of spacing with tank body (15) bottom, in tank body (15) lower end, right side, there is charging aperture, in upper end, tank body (15) left side, have discharging opening, the charging aperture of described tank body (15) and discharging opening are fixedly installed togather with hot deionized water pipeline (4) respectively.
3. chemical industry still mixing device according to claim 2, is characterized in that, the hinged baffle plate (18) that is left low right high shape that is provided with in left side of described upper spacer (16), and the left end height of described baffle plate (18) is lower than the height of discharging opening.
4. according to the chemical industry still mixing device described in claim 1 or 2 or 3, it is characterized in that, described kettle (1) bottom is installed with agitator (19), and the stirring end of described agitator (19) is positioned at kettle (1).
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201420290256.6U CN203916658U (en) | 2014-05-15 | 2014-05-15 | Chemical industry still mixing device |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201420290256.6U CN203916658U (en) | 2014-05-15 | 2014-05-15 | Chemical industry still mixing device |
Publications (1)
| Publication Number | Publication Date |
|---|---|
| CN203916658U true CN203916658U (en) | 2014-11-05 |
Family
ID=51812539
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| CN201420290256.6U Expired - Fee Related CN203916658U (en) | 2014-05-15 | 2014-05-15 | Chemical industry still mixing device |
Country Status (1)
| Country | Link |
|---|---|
| CN (1) | CN203916658U (en) |
Cited By (1)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN109908851A (en) * | 2017-12-12 | 2019-06-21 | 巴斯夫新材料有限公司 | Polymer reactor |
-
2014
- 2014-05-15 CN CN201420290256.6U patent/CN203916658U/en not_active Expired - Fee Related
Cited By (1)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN109908851A (en) * | 2017-12-12 | 2019-06-21 | 巴斯夫新材料有限公司 | Polymer reactor |
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Legal Events
| Date | Code | Title | Description |
|---|---|---|---|
| C14 | Grant of patent or utility model | ||
| GR01 | Patent grant | ||
| CF01 | Termination of patent right due to non-payment of annual fee |
Granted publication date: 20141105 Termination date: 20150515 |
|
| EXPY | Termination of patent right or utility model |