CN203525599U - Defoamer diluting reaction kettle - Google Patents
Defoamer diluting reaction kettle Download PDFInfo
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- CN203525599U CN203525599U CN201320662618.5U CN201320662618U CN203525599U CN 203525599 U CN203525599 U CN 203525599U CN 201320662618 U CN201320662618 U CN 201320662618U CN 203525599 U CN203525599 U CN 203525599U
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- defoamer
- diluting
- kettle
- still
- diluting reaction
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Abstract
The utility model relates to the field of chemical equipment and discloses a defoamer diluting reaction kettle. The defoamer diluting reaction kettle comprises a diluting kettle and two vacuum homogenizing emulsification pumps, wherein the two vacuum homogenizing emulsification pumps are respectively arranged on the two sides of the diluting kettle, an inlet is communicated with the bottom end of the diluting kettle through a pipeline, an outlet is communicated with the top end of the diluting kettle, a paddle type stirring mechanism is arranged at the center of the diluting kettle, upper, middle and lower stirring paddles are arranged on the paddle type stirring mechanism, and the number of the middle stirring paddles is less than that of the upper stirring paddles and the lower stirring paddles. The defoamer diluting reaction kettle is simple in structure, novel in design and high in diluting efficiency, a thixotropic agent and a defoamer are added into the diluting kettle, the defoamer is uniformly dispersed in the defoamer due to the effect of the vacuum homogenizing emulsification pumps, the emulsification effect is good, an obtained defoamer product is high in quality, and the time needed in the production process is short.
Description
Technical field
The utility model relates to chemical industry equipment field, relates in particular to a kind of defoamer diluting reaction still.
Background technology
In many industrial production, foam is ubiquitous phenomenon and a problem, so defoamer is familiar with by people gradually for the importance of guaranteeing industrial production high-efficiency operation.In recent years, defoamer is applied in the industrial production such as petrochemical industry, pulping and paper-making, textile printing and dyeing, food processing, pharmacy fermentation, coating and printing ink, water treatment more and more widely.
In defoamer production technology, after synthetic reaction, need to add thixotropic agent to dilute, existing technology is that thixotropic agent is added drop-wise in dilution still, by paddle, be uniformly mixed, it is inhomogeneous that the shortcoming of this way is that thixotropic agent disperses in reactor, emulsifying effectiveness is bad, and poor product quality, in order to address this problem, mixing kettle in the middle of often needing to increase, in middle mixing kettle, first thixotropic agent and part defoamer are mixed, and then join in dilution still, mix with all the other defoamers, its complex process, and required dilution time is long.
Utility model content
In order to solve above technical problem, the utility model provides a kind of defoamer diluting reaction still, simple in structure, can effectively dilute emulsification defoamer, and production efficiency is high.
Complete skill scheme of the present utility model is: a kind of defoamer diluting reaction still, comprises dilution still and two vacuum homogenizing emulsifying pumps.
Described two vacuum homogenizing emulsifying pumps are arranged at respectively the both sides of dilution still, and entrance dilutes the bottom of still by pipeline connection, and outlet is communicated with the top of dilution still.
Preferably, described dilution still center is provided with paddle mixer structure.
Further, described paddle mixer structure is provided with three groups of stirrer paddles of upper, middle and lower, and in the middle of it, the stirrer paddle quantity of one group is than upper and lower two groups few one.
The utility model compared with prior art has following beneficial effect:
The utility model provides a kind of defoamer diluting reaction still, thixotropic agent and defoamer are made an addition in dilution still, utilize the effect of vacuum homogenizing emulsifying pump, thixotropic agent is uniformly dispersed in defoamer, emulsify well utilizes rabbling mechanism to make the more even of thixotropic agent dispersion in the process of dilution.Three groups of stirrer paddles due to rabbling mechanism, middle one group than upper and lower two groups few one blades, make the stir speed (S.S.) of three layers of upper, middle and lowers different, it is fiercer to make to stir, and promotes that mixing is more even, and the utility model adopts two vacuum homogenizing emulsifying pump configurations, efficiency and the effect of emulsification have been improved greatly, under the effect of vacuum homogenizing emulsifying pump, drive mixed liquor to think that by diluting still upper end lower end is mobile simultaneously, coordinate the effect of stirrer paddle further to improve the efficiency being uniformly mixed.The utility model is simple in structure, modern design, and dilution efficiency is high, emulsify well, the defoamer product quality obtaining is high, and production process required time is short.
Accompanying drawing explanation
Accompanying drawing described herein is used to provide further understanding of the present utility model, forms the application's a part, does not form to improper restriction of the present utility model, in the accompanying drawings:
Fig. 1 is the utility model structural representation.
The specific embodiment
Below in conjunction with accompanying drawing and specific embodiment, describe the utility model in detail, in this illustrative examples of the present utility model and explanation, be used for explaining the utility model, but not as to restriction of the present utility model.
The present embodiment
The present embodiment provides a kind of defoamer diluting reaction still, and structure as shown in Figure 1, comprises dilution still 1 and two vacuum homogenizing emulsifying pumps 2; Described two vacuum homogenizing emulsifying pumps 2 are arranged at respectively the both sides of dilution still 1, and entrance dilutes the bottom of still 1 by pipeline connection, and outlet is communicated with the top of dilution still 1; Described dilution still 1 center is provided with paddle mixer structure 3; Described paddle mixer structure 3 is provided with three groups of stirrer paddles 4 of upper, middle and lower, and its stirrer paddle quantity of upper and lower two groups is respectively 3, and middle one group is 2.
When the defoamer diluting reaction still of the present embodiment is applied, thixotropic agent and defoamer are made an addition in dilution still 1, utilize the effect of vacuum homogenizing emulsifying pump 2, thixotropic agent is uniformly dispersed in defoamer, emulsify well utilizes paddle mixer structure 3 to make the more even of thixotropic agent dispersion in the process of dilution.Three groups of stirrer paddles 4 due to paddle mixer structure 3, middle one group than upper and lower two groups few one blades, make the stir speed (S.S.) of three layers of upper, middle and lowers different, it is fiercer to make to stir, and promotes that mixing is more even, and the utility model adopts two vacuum homogenizing emulsifying pump configurations, efficiency and the effect of emulsification have been improved greatly, under the effect of vacuum homogenizing emulsifying pump 2, drive mixed liquor to think that by diluting still upper end lower end is mobile simultaneously, coordinate the effect of stirrer paddle 4 further to improve the efficiency being uniformly mixed.
The technical scheme above the utility model embodiment being provided is described in detail, applied specific case herein the principle of the utility model embodiment and embodiment are set forth, the explanation of above embodiment is only applicable to help to understand the principle of the utility model embodiment; , for one of ordinary skill in the art, according to the utility model embodiment, in the specific embodiment and range of application, all will change, in sum, this description should not be construed as restriction of the present utility model meanwhile.
Claims (3)
1. a defoamer diluting reaction still, comprise dilution still and two vacuum homogenizing emulsifying pumps, it is characterized in that: described two vacuum homogenizing emulsifying pumps are arranged at respectively the both sides of dilution still, and entrance dilutes the bottom of still by pipeline connection, outlet is communicated with the top of dilution still.
2. a kind of defoamer diluting reaction still according to claim 1, is characterized in that: described dilution still center is provided with paddle mixer structure.
3. a kind of defoamer diluting reaction still according to claim 2, is characterized in that: described paddle mixer structure is provided with three groups of stirrer paddles of upper, middle and lower, and in the middle of it, the stirrer paddle quantity of one group is than upper and lower two groups few one.
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201320662618.5U CN203525599U (en) | 2013-10-25 | 2013-10-25 | Defoamer diluting reaction kettle |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201320662618.5U CN203525599U (en) | 2013-10-25 | 2013-10-25 | Defoamer diluting reaction kettle |
Publications (1)
| Publication Number | Publication Date |
|---|---|
| CN203525599U true CN203525599U (en) | 2014-04-09 |
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| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| CN201320662618.5U Expired - Fee Related CN203525599U (en) | 2013-10-25 | 2013-10-25 | Defoamer diluting reaction kettle |
Country Status (1)
| Country | Link |
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| CN (1) | CN203525599U (en) |
Cited By (1)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN107551886A (en) * | 2017-09-30 | 2018-01-09 | 江阴市南丰科技有限公司 | A kind of Chemical Manufacture agitator tank |
-
2013
- 2013-10-25 CN CN201320662618.5U patent/CN203525599U/en not_active Expired - Fee Related
Cited By (1)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN107551886A (en) * | 2017-09-30 | 2018-01-09 | 江阴市南丰科技有限公司 | A kind of Chemical Manufacture agitator tank |
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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: 20140409 Termination date: 20191025 |
|
| CF01 | Termination of patent right due to non-payment of annual fee |