CN207576425U - A kind of carbonization reactor of energy-saving production calcium carbonate superfine powder - Google Patents
A kind of carbonization reactor of energy-saving production calcium carbonate superfine powder Download PDFInfo
- Publication number
- CN207576425U CN207576425U CN201721574243.1U CN201721574243U CN207576425U CN 207576425 U CN207576425 U CN 207576425U CN 201721574243 U CN201721574243 U CN 201721574243U CN 207576425 U CN207576425 U CN 207576425U
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- CN
- China
- Prior art keywords
- calcium carbonate
- energy
- tank body
- superfine powder
- carbon dioxide
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- 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.)
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Abstract
The utility model discloses a kind of carbonization reactors of energy-saving production calcium carbonate superfine powder, including support post, tank body, gas distributor, air inlet pipe, air outlet pipe, feed pipe, discharge nozzle, by the connection of each component, achieve the purpose that reduce carbonization time, improve utilization rate of carbon dioxide, reduce energy consumption；Slurry is atomized by feed pipe, high-pressure carbon dioxide gas is passed through gas distributor from air inlet pipe, make the high-pressure area of the carbon dioxide gas formation upward shape of spiral through high pressure gas nozzle, the slurry after atomization is made to be sufficiently mixed, be carbonized with carbon dioxide gas, material is flowed out from discharge nozzle later, in carbonisation is mixed, extra carbon dioxide gas is discharged through air outlet pipe, recycling is carried out, the Carbonate Particle Size being carbonized through the utility model is uniform, carbonization time is fast, efficient.
Description
Technical field
The utility model is related to calcium carbonate production equipment field, specially a kind of carbonization of energy-saving production calcium carbonate superfine powder
Reactor.
Background technology
The production preparation of calcium carbonate needs to use carbonization reactor, and existing precipitated calcium carbonate carbonization reactor, is direct
Carbon dioxide is squeezed into carbonization reactor, bubble volume is bigger, makes the precipitated calcium carbonate granularity ultimately generated bigger, right
The utilization rate of carbon dioxide is low, and carbonization time is long, precipitated calcium carbonate poor quality, this greatly affected the application of calcium carbonate later stage
Stability is badly in need of a kind of carbonization reactor of calcium carbonate superfine powder that is energy-saving, improving utilization rate of carbon dioxide.
Utility model content
Carbonization time length, the utilization to carbon dioxide when the purpose of this utility model is to solve calcium carbonate superfine powder production
The problem of rate is low provides a kind of carbonization reactor of energy-saving production calcium carbonate superfine powder, has that energy consumption is low, carbon dioxide is sharp
With rate it is high the characteristics of.
To achieve the above object, the utility model provides following technical solution：A kind of energy-saving production calcium carbonate superfine powder
Carbonization reactor, including support post, tank body, gas distributor, air inlet pipe, air outlet pipe, feed pipe, discharge nozzle, the tank body
Lower end outside is connect with support post upper end, and is all provided with temperature sensor in tank interior, for being carried out to tank interior temperature
Detection, the gas distributor is installed on tank interior, is ring-shaped, and inner ring is provided with high pressure gas nozzle, it is described into
Expects pipe is installed on tank body crown center position, and the air inlet pipe is installed on tank body side, the through-hole and gas opened up by tank body
Distributor connects, and high-pressure carbon dioxide gas is provided for gas distributor, and described air outlet pipe one end is connect with tank body upper end side,
The discharge nozzle upper end is connect with tank base centre position.
Preferably, the high pressure gas nozzle makes gas distributor baric area form spiral upward to tilt upward installation
The baric area of shape.
Preferably, the gas distributor is two layers of setting.
Preferably, the temperature sensor uses digital display type temperature sensor.
Preferably, the feed pipe lower end is atomizer.
It is same as the prior art or the prior art can be used realized that part is not directed in the device.
Compared with prior art, the beneficial effects of the utility model are as follows：A kind of carbon of energy-saving production calcium carbonate superfine powder
Change reactor, including support post, tank body, gas distributor, air inlet pipe, air outlet pipe, feed pipe, discharge nozzle, pass through each component
Connection, achieve the purpose that reduce carbonization time, improve utilization rate of carbon dioxide, reduce energy consumption.
Description of the drawings
Fig. 1 is a kind of carbonization reactor overall structure schematic cross-sectional view of energy-saving production calcium carbonate superfine powder；
Fig. 2 is a kind of carbonization reactor overall structure schematic top plan view of energy-saving production calcium carbonate superfine powder；
Fig. 3 is a kind of carbonization reactor gas distributor schematic diagram of energy-saving production calcium carbonate superfine powder；
Fig. 4 is a kind of carbonization reactor high pressure gas nozzle schematic diagram of energy-saving production calcium carbonate superfine powder.
Figure label:1 be support post, 2 be tank body, 3 be gas distributor, 4 be air inlet pipe, 5 be air outlet pipe, 6 be into
Expects pipe, 7 are discharge nozzle.
Specific embodiment
The following is a combination of the drawings in the embodiments of the present utility model, and the technical scheme in the embodiment of the utility model is carried out
It clearly and completely describes, it is clear that the described embodiments are only a part of the embodiments of the utility model rather than whole
Embodiment, based on the embodiment in the utility model, those of ordinary skill in the art are without making creative work
All other embodiments obtained shall fall within the protection scope of the present invention.
In the description of the present invention, it is to be appreciated that term " on ", " under ", "front", "rear", "left", "right",
The orientation or position relationship of the instructions such as " top ", " bottom ", " interior ", " outer " are based on orientation shown in the drawings or position relationship, are only
The utility model must have specific with the device or element for simplifying description rather than instruction or hint meaning for ease of description
Orientation, with specific azimuth configuration and operation, therefore it is not intended that limitation to the utility model.
- 4 are please referred to Fig.1, a kind of carbonization reactor of energy-saving production calcium carbonate superfine powder, including support post 1, tank body
2nd, gas distributor 3, air inlet pipe 4, air outlet pipe 5, feed pipe 6, discharge nozzle 7,2 lower end outside of tank body connect with 1 upper end of support post
It connects, and temperature sensor is all provided with inside tank body 2, for being detected to 2 internal temperature of tank body, gas distributor 3 is installed on
It is ring-shaped inside tank body 2, inner ring is provided with high pressure gas nozzle, high pressure gas nozzle makes gas to tilt upward installation
The flow area of body distributor 3 forms the high-pressure area of the upward shape of spiral, and gas distributor 3 is two layers of setting, and feed pipe 6 is pacified
Atomizer is set loaded on 2 crown center position of tank body, and in lower end, air inlet pipe 4 is installed on 2 side of tank body, passes through tank body 2
The through-hole opened up is connect with gas distributor 3, and high-pressure carbon dioxide gas, 5 one end of air outlet pipe and tank are provided for gas distributor 3
2 upper end side of body connects, and 7 upper end of discharge nozzle is connect with 2 bottom centre position of tank body.
In summary：A kind of carbonization reactor of energy-saving production calcium carbonate superfine powder, including support post 1, tank body 2, gas
Body distributor 3, air inlet pipe 4, air outlet pipe 5, feed pipe 6, discharge nozzle 7, by the connection of each component, reach reduce carbonization time,
Improve utilization rate of carbon dioxide, the purpose for reducing energy consumption；Slurry is atomized by feed pipe 6, by high-pressure carbon dioxide
Gas is passed through gas distributor 3 from air inlet pipe 4, and the high gas of the carbon dioxide gas formation upward shape of spiral is made through high pressure gas nozzle
Pressure area makes the slurry after atomization be sufficiently mixed, be carbonized with carbon dioxide gas, and material is flowed out from discharge nozzle 7 later, in mixing carbon
During change, extra carbon dioxide gas is discharged through air outlet pipe, is carried out recycling, is carbonized through the utility model
Carbonate Particle Size is uniform, carbonization time is fast, efficient.
The basic principle of the utility model and main feature and the advantages of the utility model, one's own profession has been shown and described above
The technical staff of industry is described in the above embodiment and specification it should be appreciated that the utility model is not limited by above-mentioned implementation 1
Only illustrate the principle of the utility model, on the premise of not departing from the spirit and scope of the utility model, the utility model can also
There are various changes and modifications, these various changes and improvements fall within the scope of the claimed invention, and the utility model will
Protection domain is asked to be defined by the appending claims and its equivalent thereof.
Claims (5)
1. a kind of carbonization reactor of energy-saving production calcium carbonate superfine powder, including support post, tank body, gas distributor, air inlet
Pipe, air outlet pipe, feed pipe, discharge nozzle, the tank body lower end outside are connect, and be all provided with temperature in tank interior with support post upper end
Sensor is spent, for being detected to tank interior temperature, the gas distributor is installed on tank interior, is ring-shaped,
Inner ring is provided with high pressure gas nozzle, the feed pipe is installed on tank body crown center position, and the air inlet pipe is installed on tank
Body side is connect by the through-hole that tank body opens up with gas distributor, and high-pressure carbon dioxide gas, institute are provided for gas distributor
It states air outlet pipe one end to connect with tank body upper end side, the discharge nozzle upper end is connect with tank base centre position.
2. a kind of carbonization reactor of energy-saving production calcium carbonate superfine powder according to claim 1, it is characterised in that：It is described
High pressure gas nozzle makes gas distributor baric area form the baric area of the upward shape of spiral to tilt upward installation.
3. a kind of carbonization reactor of energy-saving production calcium carbonate superfine powder according to claim 1, it is characterised in that：It is described
Gas distributor is two layers of setting.
4. a kind of carbonization reactor of energy-saving production calcium carbonate superfine powder according to claim 1, it is characterised in that：It is described
Temperature sensor uses digital display type temperature sensor.
5. a kind of carbonization reactor of energy-saving production calcium carbonate superfine powder according to claim 1, it is characterised in that：It is described
Feed pipe lower end is atomizer.
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201721574243.1U CN207576425U (en) | 2017-11-22 | 2017-11-22 | A kind of carbonization reactor of energy-saving production calcium carbonate superfine powder |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201721574243.1U CN207576425U (en) | 2017-11-22 | 2017-11-22 | A kind of carbonization reactor of energy-saving production calcium carbonate superfine powder |
Publications (1)
| Publication Number | Publication Date |
|---|---|
| CN207576425U true CN207576425U (en) | 2018-07-06 |
Family
ID=62732948
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| CN201721574243.1U Expired - Fee Related CN207576425U (en) | 2017-11-22 | 2017-11-22 | A kind of carbonization reactor of energy-saving production calcium carbonate superfine powder |
Country Status (1)
| Country | Link |
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| CN (1) | CN207576425U (en) |
Cited By (5)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN109775728A (en) * | 2019-03-22 | 2019-05-21 | 淮阴工学院 | The inlet duct of variable diameter carbonators |
| CN110252206A (en) * | 2019-06-28 | 2019-09-20 | 广西金秀松源林产有限公司 | A kind of rosin dissolver and method |
| CN111398347A (en) * | 2020-03-02 | 2020-07-10 | 武汉理工大学 | Device and method for measuring temperature rise of carbonization reaction |
| CN114917747A (en) * | 2022-05-27 | 2022-08-19 | 山东世光工业设备制造有限公司 | Storage tank with protective structure for carbon neutralization |
| CN116272330A (en) * | 2023-03-23 | 2023-06-23 | 汇舸(南通)环保设备有限公司 | Flue gas uniform distribution device and marine desulfurizing tower adopting same |
-
2017
- 2017-11-22 CN CN201721574243.1U patent/CN207576425U/en not_active Expired - Fee Related
Cited By (6)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN109775728A (en) * | 2019-03-22 | 2019-05-21 | 淮阴工学院 | The inlet duct of variable diameter carbonators |
| CN110252206A (en) * | 2019-06-28 | 2019-09-20 | 广西金秀松源林产有限公司 | A kind of rosin dissolver and method |
| CN111398347A (en) * | 2020-03-02 | 2020-07-10 | 武汉理工大学 | Device and method for measuring temperature rise of carbonization reaction |
| CN114917747A (en) * | 2022-05-27 | 2022-08-19 | 山东世光工业设备制造有限公司 | Storage tank with protective structure for carbon neutralization |
| CN116272330A (en) * | 2023-03-23 | 2023-06-23 | 汇舸(南通)环保设备有限公司 | Flue gas uniform distribution device and marine desulfurizing tower adopting same |
| CN116272330B (en) * | 2023-03-23 | 2023-10-03 | 汇舸(南通)环保设备有限公司 | Flue gas uniform distribution device and marine desulfurizing tower adopting same |
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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: 20180706 Termination date: 20181122 |
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| CF01 | Termination of patent right due to non-payment of annual fee |