CN207192824U - A kind of process units of nano-calcium carbonate - Google Patents
A kind of process units of nano-calcium carbonate Download PDFInfo
- Publication number
- CN207192824U CN207192824U CN201721012052.6U CN201721012052U CN207192824U CN 207192824 U CN207192824 U CN 207192824U CN 201721012052 U CN201721012052 U CN 201721012052U CN 207192824 U CN207192824 U CN 207192824U
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- Prior art keywords
- tower body
- nano
- calcium carbonate
- sets
- process units
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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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- Compounds Of Alkaline-Earth Elements, Aluminum Or Rare-Earth Metals (AREA)
Abstract
It the utility model is related to a kind of process units of nano-calcium carbonate,Including tower body,The tower body top sets the feed pipe of material,Dissolving,The feed pipe passes through dissolving,And stretch in tower body,The dissolving is connected by the pipeline high pressure gas holder B external with tower body,Divide two layers in the tower body,Separated by dividing plate,Upper strata sets spray canister,Feed pipe stretches into spray canister,Spray canister both sides set high-pressure spray gun,High-pressure spray gun is connected by the pipeline high pressure gas holder A external with tower body,Lower floor sets two sets of air jet systems from top to bottom,Including the fumarole on the endless metal pipe and metal tube of the fixation of tower body inwall,Collided by high-pressure spray gun strength,Make solution atomization,The gas dissolved in solution can expand because of the reduction of pressure,Secondary-atomizing,To improve carbonation rate and preventing from piling up phenomenon,Inert gas air jet system jet,Float rolling fog,It is small with the nano-calcium carbonate particles that this process units produces,Carbonation rate is high,Production efficiency is high,It is and practical.
Description
Technical field
The production equipment of nano-calcium carbonate is the utility model is related to, more particularly relates to a kind of production dress of nano-calcium carbonate
Put.
Background technology
The main production facility of nano-calcium carbonate is generally carbonization reactor, existing carbonization reactor point at present：Commonly stir
Type, continuous aerosol type and hypergravity synthesis type are mixed, aerosol type typically first sprays raw slurry spraying, then is mixed with the gas in tower body
Being reacted after conjunction, carbonation rate is higher than stirred type, but the atomizer price generally used, and easily blocks, and influences production efficiency, and
And the mixed effect and carbonation rate of the raw slurry and gas after being atomized need to be improved.
Utility model content
In view of this, the purpose of this utility model is to provide that a kind of nano-calcium carbonate particles of output are small, carbonation rate is high, raw
Produce the process units of the nano-calcium carbonate of efficiency high.
In order to solve the above technical problems, the technical solution of the utility model is：
A kind of process units of nano-calcium carbonate, including tower body, the tower body top set the feed pipe of material, dissolving,
The feed pipe passes through dissolving, and stretches in tower body, and the dissolving is connected by the external high pressure gas holder B of pipeline and tower body
Connecing, divide two layers in the tower body, separated by dividing plate, upper strata sets spray canister, and feed pipe stretches into spray canister, and spray canister both sides set high-pressure spray gun,
High-pressure spray gun is connected by the pipeline high pressure gas holder A external with tower body, and lower floor sets two sets of air jet systems from top to bottom, including surround
The fumarole on endless metal pipe and metal tube that tower body inwall is fixed.
Preferably, the angle of high-pressure spray gun and the tower body axis is between 30-45 °.
Preferably, magnetic valve B is set on the connecting pipe of the high pressure gas holder B and dissolving.
Preferably, gas distributor, gas distributor and height are set on the connecting pipe of the high pressure gas holder A and high-pressure spray gun
Calm the anger and set magnetic valve A on the connecting pipe between tank A.
Preferably, the air jet system, above it is a set of be carbon dioxide air jet system, below it is a set of be inert gas jet
Device.
Preferably, the tower body bottom sets valve export.
The beneficial effects of the utility model：By in the solution that dissolves in gas to feed pipe in dissolving, then spraying
Cylinder in, using high-pressure spray gun strength collide, make solution atomization, the gas dissolved in solution because the reduction of pressure can expand, so as to
Secondary-atomizing is formed, carbon dioxide air jet system sprays gas, compatible with atomized liquid, reaction, to improve carbonation rate and preventing heap
Poly- phenomenon, inert gas air jet system jet, float rolling fog, with this process units produce nano-calcium carbonate particles it is small,
Carbonation rate is high, production efficiency is high and practical.
Brief description of the drawings
Fig. 1：The utility model structure diagram；
Wherein：1st, valve export；2nd, fumarole；3rd, metal tube；4th, gas distributor；5th, magnetic valve A；6th, high pressure gas holder A；
7th, high pressure gas holder B；8th, magnetic valve B；9th, pipeline；10th, dissolving；11st, feed pipe；12nd, high-pressure spray gun；13rd, spray canister；14th, tower body；
15th, dividing plate.
Embodiment
Below in conjunction with accompanying drawing, specific embodiment of the present utility model is described in further detail, so that the utility model skill
Art scheme is more readily understood and grasped.
Embodiment 1
As shown in figure 1, material is welded on a kind of process units of nano-calcium carbonate, including tower body 14, the top of tower body 14
Feed pipe 11, dissolving 10, feed pipe 11 feed pipe 11 and stretched into through dissolving 10 and the gas that dissolves in dissolving 10
To tower body 14, the dissolving 10 is connected by the high pressure gas holder B7 external with tower body 14 of pipeline 9, high pressure gas holder B7 and molten gas
Magnetic valve B8 is set on the connecting pipe of tank 10, divides two layers in the tower body 14, is separated by dividing plate 15, upper strata sets spray canister 13, spray canister
13 are fixed on dividing plate 15, and in the perforate of dividing plate 15, spray canister 13 is connected lower floor, and feed pipe 11 stretches into spray canister 13,13 liang of spray canister
Side sets high-pressure spray gun 12, and the angle of high-pressure spray gun 12 and the axis of tower body 14 is 45 °, and high-pressure spray gun 12 passes through pipeline 9 and tower body 14
External high pressure gas holder A6 connections, high pressure gas holder A6 is with setting gas distributor 4, gas distribution on the connecting pipe of high-pressure spray gun 12
Magnetic valve A5 is set on connecting pipe between device 4 and high pressure gas holder A6, gas distributor 4 distributes gas to two high-pressure spray guns
12, lower floor sets two sets of air jet systems from top to bottom, including on the endless metal pipe 3 and metal tube 3 that the inwall of tower body 14 is fixed
Fumarole 2, wherein above it is a set of is carbon dioxide air jet system, below it is a set of be inert gas air jet system.
The bottom of tower body 14 sets valve export 1.
The utility model is by the solution that dissolves in gas to feed pipe 11 in dissolving 10, then in spray canister 13,
Strongly collided using high-pressure spray gun 12, make solution atomization, the gas dissolved in solution is because the reduction of pressure can expand, so as to be formed
Secondary-atomizing, carbon dioxide air jet system sprays gas, compatible with atomized liquid, reaction, to improve carbonation rate and preventing from piling up now
As, inert gas air jet system jet, float rolling fog, so that the nano-calcium carbonate particles that this process units produces are small, carbonization
Rate is high, production efficiency is high and practical.
Certainly, it the above is only concrete application example of the present utility model, the scope of protection of the utility model do not formed and appointed
What is limited.All technical schemes formed using equivalent transformation or equivalent replacement, all fall within the utility model rights protection model
Within enclosing.
Claims (6)
1. a kind of process units of nano-calcium carbonate, including tower body, it is characterised in that the tower body top sets the charging of material
Pipe, dissolving, the feed pipe passes through dissolving, and stretches in tower body, and the dissolving is external by pipeline and tower body
High pressure gas holder B connections, the tower body is interior to be divided two layers, is separated by dividing plate, upper strata sets spray canister, and feed pipe stretches into spray canister, spray canister both sides
If high-pressure spray gun, high-pressure spray gun is connected by the pipeline high pressure gas holder A external with tower body, and lower floor sets two sets of jet dresses from top to bottom
Put, including the fumarole on the endless metal pipe and metal tube that tower body inwall is fixed.
2. the process units of a kind of nano-calcium carbonate according to claim 1, it is characterised in that the high-pressure spray gun and tower
The angle of body axis is between 30-45 °.
A kind of 3. process units of nano-calcium carbonate according to claim 1, it is characterised in that the high pressure gas holder B with
Magnetic valve B is set on the connecting pipe of dissolving.
A kind of 4. process units of nano-calcium carbonate according to claim 1, it is characterised in that the high pressure gas holder A with
Gas distributor is set on the connecting pipe of high-pressure spray gun, electromagnetism is set on the connecting pipe between gas distributor and high pressure gas holder A
Valve A.
A kind of 5. process units of nano-calcium carbonate according to claim 1, it is characterised in that the air jet system, on
A set of face is carbon dioxide air jet system, below it is a set of be inert gas air jet system.
6. the process units of a kind of nano-calcium carbonate according to claim 1, it is characterised in that the tower body bottom sets valve
Door outlet.
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201721012052.6U CN207192824U (en) | 2017-08-14 | 2017-08-14 | A kind of process units of nano-calcium carbonate |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201721012052.6U CN207192824U (en) | 2017-08-14 | 2017-08-14 | A kind of process units of nano-calcium carbonate |
Publications (1)
| Publication Number | Publication Date |
|---|---|
| CN207192824U true CN207192824U (en) | 2018-04-06 |
Family
ID=61797599
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| CN201721012052.6U Expired - Fee Related CN207192824U (en) | 2017-08-14 | 2017-08-14 | A kind of process units of nano-calcium carbonate |
Country Status (1)
| Country | Link |
|---|---|
| CN (1) | CN207192824U (en) |
Cited By (1)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN112774611A (en) * | 2021-01-18 | 2021-05-11 | 广西大学 | Hypergravity micro-interface mass transfer enhanced reaction-crystallization drying coupling all-in-one machine |
-
2017
- 2017-08-14 CN CN201721012052.6U patent/CN207192824U/en not_active Expired - Fee Related
Cited By (2)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN112774611A (en) * | 2021-01-18 | 2021-05-11 | 广西大学 | Hypergravity micro-interface mass transfer enhanced reaction-crystallization drying coupling all-in-one machine |
| CN112774611B (en) * | 2021-01-18 | 2024-01-30 | 广西大学 | Super-gravity micro-interface mass transfer strengthening reaction-crystallization drying coupling integrated machine |
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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: 20180406 Termination date: 20200814 |
|
| CF01 | Termination of patent right due to non-payment of annual fee |