CN206229344U - A kind of multistage spray carbonation tower - Google Patents
A kind of multistage spray carbonation tower Download PDFInfo
- Publication number
- CN206229344U CN206229344U CN201621136496.6U CN201621136496U CN206229344U CN 206229344 U CN206229344 U CN 206229344U CN 201621136496 U CN201621136496 U CN 201621136496U CN 206229344 U CN206229344 U CN 206229344U
- Authority
- CN
- China
- Prior art keywords
- tower body
- tower
- charging aperture
- shower nozzle
- supervisor
- Prior art date
- Legal status (The legal status is an assumption and is not a legal conclusion. Google has not performed a legal analysis and makes no representation as to the accuracy of the status listed.)
- Expired - Fee Related
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Abstract
The utility model discloses a kind of multistage spray carbonation tower, including tower body, charging aperture, discharging opening, CO2Feeding pipe and agitating device, the agitating device are fixed on the tower body top by support, and go deep into inside tower body, the CO2Feeding pipe includes CO2Branch pipe, CO2Shower nozzle and CO2Supervisor, the CO2Branch pipe is fixed with tower body annular by fix bar, and inner side is provided with the CO2Shower nozzle, it is outside with the CO2Supervisor's connection；The charging aperture is arranged at tower body upper side, is internally provided with atomizer, and outlet is fixedly connected a slurry spray nozzle.The utility model is taken and installs atomizer and shower nozzle and to CO in charging aperture on the basis of existing stirring-type carbonators2The measure that feeding manner is improved, makes CO2Gas can be fully absorbed, slurry and CO2The carburizing reagent of gas is more abundant, so as to effectively improve production efficiency.
Description
Technical field
The utility model is related to carbonators field, specifically a kind of multistage spray carbonation tower.
Background technology
Carbonators is the indispensable equipment for preparing the raw materials of industry such as activated Calcium carbonate, calcium carbonate superfine powder, soda ash, existing
Have in technology, conventional carbonators mainly has three classes such as stirring-type, continuous atomizing and hypergravity synthesis, wherein stirring-type carbonization
Tower is small because of its investment, and the condition such as reaction temperature, concentration and mixing speed is easy to control and is widely used, but such carbon
There is CO in change equipment2The shortcomings of absorbing insufficient, carbonization insufficient, reaction time long, low production efficiency, and obtained after carbonization
Carbonate product easily condense blocking, increased burden to subsequent treatment operation into discharge pipe, influence manufacturing schedule and life
Produce efficiency, it is therefore necessary to the kind equipment is improved in the hope of improving its production performance.
Utility model content
Technical problem to be solved in the utility model is to provide a kind of multistage spray carbonation tower.
In order to solve the above technical problems, a kind of multistage spray carbonation tower described in the utility model, including tower body, charging aperture, go out
Material mouth, CO2Feeding pipe and agitating device, the agitating device include agitating shaft, decelerator, motor and stirrer paddle, described
Agitating shaft is arranged inside the tower body, and its one end is connected with the decelerator, and position is fixedly connected with the agitating paddle in tower
Leaf, the decelerator and the motor connection, and the tower body top, the CO are fixed on by support2Feeding pipe includes
CO2Branch pipe, CO2Shower nozzle and CO2Supervisor, the CO2Branch pipe is fixed with tower body annular by fix bar, and inner side is provided with described
CO2Shower nozzle, it is outside with the CO2Supervisor's connection；The charging aperture is arranged at tower body upper side, is internally provided with atomizer, and
Outlet is fixedly connected a slurry spray nozzle.
Further, the tower body side is additionally provided with manhole.
Further, the tower body bottom is provided with filter and slag notch, and the filter is fixedly connected with the discharging opening.
Compared with prior art, the utility model has advantages below：
（1）The utility model is taken and installs atomizer and shower nozzle in charging aperture on the basis of existing stirring-type carbonators
With to CO2The measure that feeding manner is improved, further increases slurry and CO2The contact area of gas, makes CO2Gas energy
Enough be fully absorbed, slurry and CO2The carburizing reagent of gas is more abundant, hence it is evident that shorten the reaction time；
（2）The utility model can prevent and treat caking materials and block in tower body bottom discharge mouthful setting filter and slag notch
Shape impurity enters discharge pipe, is increased burden to subsequent handling, so as to effectively improve production efficiency；
（3）The utility model can be improved using stirring and spraying mixing two ways while energy consumption is reduced
Production efficiency, it is cost-effective, with objective market prospects.
Brief description of the drawings
Fig. 1 is structural representation of the present utility model.
In figure：1st, tower body, 2, CO2Branch pipe, 3, agitating shaft, 4, CO2Shower nozzle, 5, CO2Supervisor, 6, decelerator, 7, motor, 8,
Support, 9, atomizer, 10, charging aperture, 11, slurry spray nozzle, 12, fix bar, 13, manhole, 14, discharging opening, 15, filter, 16,
Slag notch, 17, stirrer paddle.
Specific embodiment
Illustrate to be described further the utility model below in conjunction with the accompanying drawings.
A kind of multistage spray carbonation tower as shown in Figure 1, including tower body 1, charging aperture 10, discharging opening 14, CO2Feeding pipe and stir
Device is mixed, agitating device includes agitating shaft 3, decelerator 6, motor 7 and stirrer paddle 17, and agitating shaft 3 is arranged inside tower body 1,
Its one end is connected with decelerator 6, and position is fixedly connected with stirrer paddle 17 in tower, and decelerator 6 is connected with motor 7, and by branch
Frame 8 is fixed on tower body（1）Top, CO2Feeding pipe includes CO2Branch pipe 2, CO2Shower nozzle 4 and CO2Supervisor 5, CO2Branch pipe 2 is by solid
Fixed pole 12 is fixed with the annular of tower body 1, and inner side is provided with CO2Shower nozzle 4, outside and CO2Supervisor 5 connects；Charging aperture 10 is arranged at tower body 1
Upper side, is internally provided with atomizer 9, and outlet is fixedly connected a slurry spray nozzle 11；The side of tower body 1 is additionally provided with manhole 13,
Bottom is provided with filter 15 and slag notch 16, and filter 15 is fixedly connected with discharging opening 14.
The course of work of the present utility model is as follows：During work, open the startup agitating device of motor 7 and persistently stir, while connecing
Logical CO2Supervisor 5 is passed through CO2Gas, and slurry is accessed into charging aperture 10, slurry is sprayed after being atomized through atomizer 9 by slurry spray nozzle 11
Go out, now vaporific slurry will and CO2Gas is fully contacted and carburizing reagent occurs, reaction terminate after after the removal of impurities of filter 15
Next treatment process is entered by discharging opening 14, filtering impurity or caking product can be discharged by slag notch 16.The utility model
On the basis of existing stirring-type carbonators, take and atomizer and shower nozzle are installed and to CO in charging aperture2Feeding manner is changed
Kind measure, further increases slurry and CO2The contact area of gas, makes CO2Gas can be fully absorbed, slurry and CO2
The carburizing reagent of gas is more abundant, hence it is evident that shorten the reaction time；And by tower body bottom discharge mouthful setting filter
And slag notch, caking materials can be prevented and treated and block impurity enters discharge pipe, increased burden to subsequent handling, so as to effectively carry
High efficiency；Meanwhile, the utility model, can be while energy consumption be reduced using stirring and spraying mixing two ways
Improve production efficiency, it is cost-effective, with objective market prospects.
Claims (3)
1. a kind of multistage spray carbonation tower, including tower body（1）, charging aperture（10）, discharging opening（14）、CO2Feeding pipe and agitating device,
The agitating device includes agitating shaft（3）, decelerator（6）, motor（7）And stirrer paddle（17）, the agitating shaft（3）It is arranged at
The tower body（1）Inside, its one end and the decelerator（6）Connection, position is fixedly connected with the stirrer paddle in tower（17）,
The decelerator（6）With the motor（7）Connection, and by support（8）It is fixed on the tower body（1）Top, it is characterised in that：
The CO2Feeding pipe includes CO2Branch pipe（2）、CO2Shower nozzle（4）And CO2Supervisor（5）, the CO2Branch pipe（2）By fix bar
（12）With the tower body（1）Annular is fixed, and inner side is provided with the CO2Shower nozzle（4）, it is outside with the CO2Supervisor（5）Connection；It is described
Charging aperture（10）It is arranged at tower body（1）Upper side, is internally provided with atomizer（9）, and outlet is fixedly connected a slurry spray nozzle
（11）.
2. a kind of multistage spray carbonation tower according to claim 1, it is characterised in that：The tower body（1）Side is additionally provided with manhole
（13）.
3. a kind of multistage spray carbonation tower according to claim 1, it is characterised in that：The tower body（1）Bottom is provided with filter
（15）And slag notch（16）, the filter（15）With the discharging opening（14）It is fixedly connected.
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201621136496.6U CN206229344U (en) | 2016-10-19 | 2016-10-19 | A kind of multistage spray carbonation tower |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201621136496.6U CN206229344U (en) | 2016-10-19 | 2016-10-19 | A kind of multistage spray carbonation tower |
Publications (1)
| Publication Number | Publication Date |
|---|---|
| CN206229344U true CN206229344U (en) | 2017-06-09 |
Family
ID=58982754
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| CN201621136496.6U Expired - Fee Related CN206229344U (en) | 2016-10-19 | 2016-10-19 | A kind of multistage spray carbonation tower |
Country Status (1)
| Country | Link |
|---|---|
| CN (1) | CN206229344U (en) |
Cited By (1)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN108047158A (en) * | 2017-12-20 | 2018-05-18 | 常州大学 | A kind of conversion CO, CO2For the device of isatoic anhydride |
-
2016
- 2016-10-19 CN CN201621136496.6U patent/CN206229344U/en not_active Expired - Fee Related
Cited By (2)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN108047158A (en) * | 2017-12-20 | 2018-05-18 | 常州大学 | A kind of conversion CO, CO2For the device of isatoic anhydride |
| CN108047158B (en) * | 2017-12-20 | 2021-07-27 | 常州大学 | Conversion of CO and CO2Device for producing isatoic anhydride |
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Legal Events
| Date | Code | Title | Description |
|---|---|---|---|
| GR01 | Patent grant | ||
| GR01 | Patent grant | ||
| CF01 | Termination of patent right due to non-payment of annual fee |
Granted publication date: 20170609 Termination date: 20171019 |
|
| CF01 | Termination of patent right due to non-payment of annual fee |