CN207628406U - High efficiency solid-liquid disperses reaction system - Google Patents
High efficiency solid-liquid disperses reaction system Download PDFInfo
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- CN207628406U CN207628406U CN201721645068.0U CN201721645068U CN207628406U CN 207628406 U CN207628406 U CN 207628406U CN 201721645068 U CN201721645068 U CN 201721645068U CN 207628406 U CN207628406 U CN 207628406U
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- reaction kettle
- reaction
- high efficiency
- circulating pump
- discharge nozzle
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Abstract
The utility model discloses a kind of high efficiency solid-liquids to disperse reaction system, its key points of the technical solution are that including reaction kettle and external circulating system, the external circulating system is arranged on reaction kettle, for carrying out outer loop work to the material in reaction kettle, the external circulating system includes discharge nozzle, feed pipe, cutter and circulating pump, the discharge nozzle is arranged in the lower section of reaction kettle, and it is connected in reaction kettle, the feed pipe is arranged in the top of reaction kettle, and it is connected in reaction kettle, the one end of feed inlet connection discharge nozzle far from reaction kettle of the cutter, discharge port connects the import of circulating pump, the one end of outlet feed pipe far from reaction kettle of the circulating pump, material in merging reaction kettle passes sequentially through discharge nozzle, cutter, enter in reaction kettle after circulating pump and feed pipe, form Matter Transfer.The high efficiency solid-liquid dispersion reaction system of the utility model can improve mixing efficiency, accelerate reaction rate.
Description
Technical field
The utility model is related to a kind of high efficiency solid-liquids to disperse reaction system.
Background technology
Often have in production and the reaction that solid constituent carries out is added inside liquid phase feed, for example present non-ionic surface is lived
Property agent sulfonating reaction, needs the sulfonating reaction agent for putting into solid at regular time and quantity in the nonionic surfactant of liquid phase.But
Often exist the solid phase sulfonating agent that adds be difficult to it is evenly dispersed seriously affect reactivity, when also adding, solid particle is easy
It is adhered on consersion unit, generates compared with lossy and then influence the reactivity of product, caused salt content in product high, influence
Product quality.
According to conventional consersion unit and condition, solid-liquid phase reaction reactivity is relatively low, and material loss is larger, causes product
Interior inorganic salt content is higher to be removed, and quality is influenced.The main reason for throwing into question be：（1）Solid phase is difficult by stirring merely
Paddle stirring is mixed to be uniformly dispersed in liquid phase；（2）Solid phase dispersion can precipitate and lump in reactor bottom quickly after liquid phase, lead
Cause this partial material that cannot participate in reacting；（3）When feeding intake due to, powder be easy to drift be adhered to reactor wall etc. can not be with liquid phase
The position of contact, causes material loss.
Utility model content
In view of the deficienciess of the prior art, the purpose of this utility model is to provide one kind capable of improving mixing efficiency,
The high efficiency solid-liquid of reaction rate is accelerated to disperse reaction system.
To achieve the above object, the utility model provides following technical solution：A kind of high efficiency solid-liquid dispersion reaction system,
Including reaction kettle and external circulating system, the external circulating system is arranged on reaction kettle, for being carried out to the material in reaction kettle
Outer loop works, and the external circulating system includes discharge nozzle, feed pipe, cutter and circulating pump, and the discharge nozzle setting exists
The lower section of reaction kettle, and be connected in reaction kettle, the feed pipe is arranged in the top of reaction kettle, and is connected in reaction kettle, described
The one end of feed inlet connection discharge nozzle far from reaction kettle of cutter, discharge port connect the import of circulating pump, the circulating pump
The one end of outlet feed pipe far from reaction kettle, the material being placed in reaction kettle pass sequentially through discharge nozzle, cutter, circulating pump
Enter in reaction kettle with after feed pipe, forms Matter Transfer.
The utility model is further arranged to：Infundibulate cast feeder is provided at the feeding port of the reaction kettle.
The utility model is further arranged to：The lower end of the infundibulate cast feeder is set as lengthening conduit, lengthens conduit
Lower end close to material liquid surface.
The utility model is further arranged to：The circulating pump is gear pump.
The utility model is further arranged to：The cutter is shearing dispersion machine.
The utility model is further arranged to：The discharge nozzle is provided with the first valve on one end of reaction kettle.
The utility model is further arranged to：The feed pipe is provided with the second valve on one end of reaction kettle.
The utility model tool has the advantage that：Mixing efficiency can be improved by external circulating system, accelerates reaction rate, is led to
Setting infundibulate cast feeder is crossed, material is importing directly into the closer top of liquid phase surface distance, effectively kept away by the conduit of lengthening
Material is exempted from and has drifted loss, by being combined gear pump and shearing dispersion machine, the flowing of material can have been accelerated to avoid solid-phase material
Sedimentation, and to solid powder it is further crushing and dispersion, accelerate reaction rate improve reaction efficiency.
Description of the drawings
Fig. 1 is the structural schematic diagram of the utility model.
In figure：1, reaction kettle；2, discharge nozzle；3, feed pipe；4, cutter；5, circulating pump；6, infundibulate cast feeder；7,
One valve；8, the second valve.
Specific implementation mode
Shown in referring to Fig.1, a kind of high efficiency solid-liquid of the present embodiment disperses reaction system, including reaction kettle 1 and outer circulation system
System, the external circulating system are arranged on reaction kettle 1, described outer for carrying out outer loop work to the material in reaction kettle 1
The circulatory system includes discharge nozzle 2, feed pipe 3, cutter 4 and circulating pump 5, and the discharge nozzle 2 is arranged in the lower section of reaction kettle 1,
And be connected in reaction kettle 1, the feed pipe 3 is arranged in the top of reaction kettle 1, and is connected in reaction kettle 1, the cutter 4
Feed inlet is connected to the one end of discharge nozzle 2 far from reaction kettle 1, and discharge port connects the import of circulating pump 5, the outlet of the circulating pump 5
It is connected to the one end of feed pipe 3 far from reaction kettle 1, the material being placed in reaction kettle 1 passes sequentially through discharge nozzle 2, cutter 4, cycle
Enter in reaction kettle 1 after pump 5 and feed pipe 3, forms Matter Transfer.
Infundibulate cast feeder 6 is provided at the feeding port of the reaction kettle 1.
The lower end of the infundibulate cast feeder 6 is set as lengthening conduit, lengthens the lower end of conduit close to material liquid surface.
The circulating pump 5 is gear pump.
The cutter 4 is shearing dispersion machine.
The discharge nozzle 2 is provided with the first valve 7 on one end of reaction kettle 1.
The feed pipe 3 is provided with the second valve 8 on one end of reaction kettle 1.
By using above-mentioned technical proposal, mixing efficiency can be improved by external circulating system, accelerate reaction rate, pass through
Infundibulate cast feeder 6 is set, and material is importing directly into the closer top of liquid phase surface distance by the conduit of lengthening, is effectively avoided
Material drifts loss, and by being combined gear pump and shearing dispersion machine, the flowing of material can be accelerated to avoid solid-phase material
Sedimentation, and further crushing and dispersion to solid powder, accelerate reaction rate to improve reaction efficiency.
The above is only the preferred embodiment of the utility model, and the scope of protection of the utility model is not limited merely to
Above-described embodiment, technical solution belonging to the idea of the present invention belong to the scope of protection of the utility model.It should refer to
Go out, for those skilled in the art, it is without departing from the principle of the utility model it is several improvement and
Retouching, these improvements and modifications also should be regarded as the scope of protection of the utility model.
Claims (7)
1. a kind of high efficiency solid-liquid disperses reaction system, it is characterised in that：Including reaction kettle and external circulating system, the outer circulation system
System is arranged on reaction kettle, and for carrying out outer loop work to the material in reaction kettle, the external circulating system includes discharging
Pipe, feed pipe, cutter and circulating pump, the discharge nozzle is arranged in the lower section of reaction kettle, and is connected in reaction kettle, the charging
Pipe is arranged in the top of reaction kettle, and is connected in reaction kettle, and the feed inlet of the cutter is connected to discharge nozzle far from reaction kettle
One end, discharge port connect the import of circulating pump, and the one end of outlet feed pipe far from reaction kettle of the circulating pump, merging is instead
Enter in reaction kettle after answering the material in kettle to pass sequentially through discharge nozzle, cutter, circulating pump and feed pipe, forms Matter Transfer.
2. high efficiency solid-liquid according to claim 1 disperses reaction system, it is characterised in that：At the feeding port of the reaction kettle
It is provided with infundibulate cast feeder.
3. high efficiency solid-liquid according to claim 2 disperses reaction system, it is characterised in that：Under the infundibulate cast feeder
End is set as lengthening conduit, lengthens the lower end of conduit close to material liquid surface.
4. high efficiency solid-liquid according to claim 1 disperses reaction system, it is characterised in that：The circulating pump is gear pump.
5. high efficiency solid-liquid according to claim 1 disperses reaction system, it is characterised in that：The cutter is that shearing disperses
Machine.
6. high efficiency solid-liquid according to claim 1 disperses reaction system, it is characterised in that：The discharge nozzle is close to reaction kettle
One end on be provided with the first valve.
7. high efficiency solid-liquid according to claim 1 disperses reaction system, it is characterised in that：The feed pipe is close to reaction kettle
One end on be provided with the second valve.
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201721645068.0U CN207628406U (en) | 2017-11-30 | 2017-11-30 | High efficiency solid-liquid disperses reaction system |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201721645068.0U CN207628406U (en) | 2017-11-30 | 2017-11-30 | High efficiency solid-liquid disperses reaction system |
Publications (1)
| Publication Number | Publication Date |
|---|---|
| CN207628406U true CN207628406U (en) | 2018-07-20 |
Family
ID=62855231
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| CN201721645068.0U Active CN207628406U (en) | 2017-11-30 | 2017-11-30 | High efficiency solid-liquid disperses reaction system |
Country Status (1)
| Country | Link |
|---|---|
| CN (1) | CN207628406U (en) |
Cited By (1)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN117619238A (en) * | 2023-12-01 | 2024-03-01 | 深圳市尚水智能股份有限公司 | Dispersion system |
-
2017
- 2017-11-30 CN CN201721645068.0U patent/CN207628406U/en active Active
Cited By (1)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN117619238A (en) * | 2023-12-01 | 2024-03-01 | 深圳市尚水智能股份有限公司 | Dispersion system |
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Legal Events
| Date | Code | Title | Description |
|---|---|---|---|
| GR01 | Patent grant | ||
| GR01 | Patent grant | ||
| CB03 | Change of inventor or designer information |
Inventor after: Hong Jian Inventor after: Song Jia Inventor after: Cui Dongjie Inventor before: Hong Jian Inventor before: Song Jia Inventor before: Cui Dongzhi |
|
| CB03 | Change of inventor or designer information |