CN206063839U - A kind of crystallizer - Google Patents
A kind of crystallizer Download PDFInfo
- Publication number
- CN206063839U CN206063839U CN201620949716.0U CN201620949716U CN206063839U CN 206063839 U CN206063839 U CN 206063839U CN 201620949716 U CN201620949716 U CN 201620949716U CN 206063839 U CN206063839 U CN 206063839U
- Authority
- CN
- China
- Prior art keywords
- stirring vane
- tank body
- crystallizer
- shaft
- capping
- 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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- Mixers Of The Rotary Stirring Type (AREA)
Abstract
A kind of crystallizer, including tank body, tank base is the taper bucket, tank body top is provided with capping, and capping top is provided with motor, and motor connection shaft is stretched in tank body, upper and lower stirring vane is provided with shaft, upper strata stirring vane is arranged in the middle part of tank body, and lower floor's stirring vane is arranged in the taper bucket, and upper strata stirring vane periphery is provided with baffle plate.Simple structure, cost-effective, solid-liquid mix homogeneously, and effectively prevent blocking.
Description
Technical field
This utility model is related to crystallizer.
Background technology
Crystallizer (thickener) use range in the market extensively, can be used for food, wine brewing, medicine, chemical industry etc.
Need the industry of crystalline particle.Thickener is common auxiliary equipment in crystallization process, is mainly used to improve the solid ratio of magma,
Particle ripening is also functioned to simultaneously and further consumes the effect of the degree of supersaturation remained in magma.But many existing knots for using
Brilliant tank (thickener) structure gaps and omissions, lacks effectively heat exchange and the effect of solid-liquid suspension, for the use of special material is not played
Good effect, for example, cool down the zinc sulfate of easy structure.
Existing crystallizer (thickener) has that heat exchange efficiency is not high, and feed liquid solid-liquid is uneven and bucket wall fouling is asked
Topic, inside crystallizer in whipping process, is susceptible to phenomenon of turning round and round so that material liquid follows impeller rotation closely, between each layer liquid
There is no axial backmixing, reduce mixing effect so that material liquid occurs lamination, the solid particle for making is got rid of to kettle wall or heavy
Sink into bottom.Turn round and round and also result in that power of agitator is unstable, so as to aggravate agitator
Vibration and shaft wear and tear.
The content of the invention
This utility model is directed to the deficiencies in the prior art, there is provided a kind of simple structure, cost-effective, and solid-liquid mixing is equal
It is even, and effectively prevent the crystallizer for blocking.
To realize this utility model purpose, there is provided technical scheme below：A kind of crystallizer, it is characterised in that including tank
Body, tank base is the taper bucket, and tank body top is provided with capping, and capping top is provided with motor, and motor connection is stirred
Mix shaft extension to enter in tank body, on shaft, be provided with upper and lower stirring vane, upper strata stirring vane is arranged in the middle part of tank body, lower floor's stirring
Blade is arranged in the taper bucket, and upper strata stirring vane periphery is provided with baffle plate.
Preferably, upper strata stirring vane outermost diameter is more than lower floor's stirring vane outermost diameter.
Preferably, shaft is eccentrically mounted in tank body.
Preferably, being evenly equipped with mesh in capping.
Preferably, the taper of the taper bucket is 30 ~ 45 °.
Preferably, levels stirring vane is provided with 2 blades, 2 blades are staggered around the center of circle.
Preferably, the nearly upper end of shaft is arranged with guide shell.
No matter the stirring is applied to the stirring of high viscosity liquid for Newton type fluid or non-Newtonian fluid, can
Strengthen mixing effect mix homogeneously.
This utility model beneficial effect：This utility model arranges upper and lower Double-blade type stirring, and selects eccentrically mounted.On
Lower pair of stirring can reduce feed liquid layering, while bottom large particle crystal can also be stirred so that feelings are blocked when blowing
Condition is reduced, and simple structure is cost-effective, solid-liquid mix homogeneously, and effectively prevents blocking.
Description of the drawings
Fig. 1 is structural representation of the present utility model.
Specific embodiment
Embodiment 1：A kind of crystallizer, including tank body 1,1 bottom of tank body are the taper bucket 2, and 1 top of tank body is provided with capping 3,
Motor 4 is installed above capping 3, the connection shaft 5 of motor 4 is stretched in tank body 1, is provided with up and down on shaft 4
Stirring vane（6、7）, upper strata stirring vane 6 is arranged in the middle part of tank body 1, and lower floor's stirring vane sets 7 and is placed in the taper bucket 2, upper strata
6 periphery of stirring vane is provided with stabilizing feed well 8.Stirring vane 6 outermost diameter in upper strata is straight more than 7 outermost of lower floor's stirring vane
Footpath.Shaft 5 is eccentrically mounted in tank body 1.Mesh 3.1 is evenly equipped with capping 3.The taper of the taper bucket 2 is 30 ~ 45 °.Levels
Stirring vane（6、7）2 blades are provided with, 2 blades are staggered around the center of circle.
Claims (7)
1. a kind of crystallizer, it is characterised in that including tank body, tank base are the taper bucket, and tank body top is provided with capping, covers
Top is provided with motor, and motor connection shaft is stretched in tank body, and upper and lower stirring vane is provided with shaft, on
Layer stirring vane is arranged in the middle part of tank body, and lower floor's stirring vane is arranged in the taper bucket, and upper strata stirring vane periphery is provided with gear
Plate.
2. a kind of crystallizer according to claim 1, it is characterised in that upper strata stirring vane outermost diameter is more than lower floor
Stirring vane outermost diameter.
3. a kind of crystallizer according to claim 1, it is characterised in that shaft is eccentrically mounted in tank body.
4. a kind of crystallizer according to claim 1, it is characterised in that mesh is evenly equipped with capping.
5. a kind of crystallizer according to claim 1, it is characterised in that the taper of the taper bucket is 30 ~ 45 °.
6. a kind of crystallizer according to claim 1, it is characterised in that levels stirring vane is provided with 2 blades, 2
Piece blade is staggered around the center of circle.
7. a kind of crystallizer according to claim 1, it is characterised in that the nearly upper end of shaft is arranged with guide shell.
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201620949716.0U CN206063839U (en) | 2016-08-26 | 2016-08-26 | A kind of crystallizer |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201620949716.0U CN206063839U (en) | 2016-08-26 | 2016-08-26 | A kind of crystallizer |
Publications (1)
| Publication Number | Publication Date |
|---|---|
| CN206063839U true CN206063839U (en) | 2017-04-05 |
Family
ID=58432580
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| CN201620949716.0U Expired - Fee Related CN206063839U (en) | 2016-08-26 | 2016-08-26 | A kind of crystallizer |
Country Status (1)
| Country | Link |
|---|---|
| CN (1) | CN206063839U (en) |
Cited By (1)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN106422397A (en) * | 2016-08-26 | 2017-02-22 | 海洲环保集团有限公司 | Crystallizing tank |
-
2016
- 2016-08-26 CN CN201620949716.0U patent/CN206063839U/en not_active Expired - Fee Related
Cited By (1)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN106422397A (en) * | 2016-08-26 | 2017-02-22 | 海洲环保集团有限公司 | Crystallizing tank |
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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: 20170405 Termination date: 20210826 |
|
| CF01 | Termination of patent right due to non-payment of annual fee |