CN205308521U - Spiral drying device is smashed in succession to crystal - Google Patents
Spiral drying device is smashed in succession to crystal Download PDFInfo
- Publication number
- CN205308521U CN205308521U CN201520962244.8U CN201520962244U CN205308521U CN 205308521 U CN205308521 U CN 205308521U CN 201520962244 U CN201520962244 U CN 201520962244U CN 205308521 U CN205308521 U CN 205308521U
- Authority
- CN
- China
- Prior art keywords
- spiral
- drying baker
- drying cabinet
- screw feeding
- crush box
- 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 relates to a spiral drying device is smashed in succession to crystal, including smashing the case, drying cabinet and conveyer, crushing case is located the drying cabinet top, smash case and drying cabinet intercommunication, it is cylindric box with the drying cabinet to smash the case, and it is the same with the drying cabinet diameter to smash the case, it is equipped with the dog -house to smash case upper portion, crushing case middle part is equipped with the spiral and smashes axle group, drying cabinet central authorities are equipped with the center pillar, the center pillar encircles and is equipped with the spiral delivery sheet, the spiral delivery sheet outside is higher than the inboard, spiral delivery sheet outside zonulae occludens is on the drying cabinet lateral wall, the drying cabinet inboard is equipped with the air heater, conveyer sets up in the drying cabinet below, spiral delivery sheet end -to -end connection conveyer. The beneficial effects of the utility model are that: smash and the drying of crystal class are gone on simultaneously, and the process is more swift, and the operating procedure is simple, and the crystal powder after the spiral transfer structure is avoided smashing glues on dry tank wall, makes the orderly conveying of crystal powder to increased drying efficiency, it is extravagant to reduce the raw materials.
Description
Technical field
This utility model belongs to chemical production equipment field, especially relates to a kind of crystal continuous and pulverizes spiral drier.
Background technology
The operation principle of crystal pulverizer series: be that material is reached to pulverize by the blade strike effect of high-speed motion in crushing chamber body, then pass through the screen cloth process to pocket. Wherein simple strike pulverize advantage be this type for chemical industry, slightly containing the pulverizing bright spot of oils and fats beans material. In usual chemical material more or less containing a certain amount of sodium so that chemical material has certain viscosity and easily polymerizable. The pure strike principle of crystal pulverizer is because of high speed pulverization, and material contact surface is little, and yield is high and solves this type of pulverizing problem very well. Generally minicrystal pulverizer is provided with screen cloth in feed bin bottom.
Some crystal is to be formed after crystallization, or is prone to the composition of deliquescence caking, and this crystalloid easily causes screen plugging situation when pulverizing, also easy corrosion and damage reducing mechanism.
Summary of the invention
For solving above-mentioned technical problem, this utility model provides a kind of crystal continuous to pulverize spiral drier.
The technical solution adopted in the utility model is: crystal continuous pulverizes spiral drier, including crush box, drying baker and transporter, crush box is positioned at above drying baker, crush box connects with drying baker, crush box and drying baker are cylindric casing, and crush box is identical with drying baker diameter, crush box top is provided with dog-house, it is provided with spiral in the middle part of crush box and smashes axle group, drying baker central authorities are provided with center pillar, center pillar is around being provided with screw feeding plate, higher than inner side outside screw feeding plate, it is close-coupled on drying baker sidewall outside screw feeding plate, hot-air blower it is provided with inside drying baker, transporter is arranged at below drying baker, screw feeding plate end connects transporter.
Preferably, screw feeding plate smooth surface, screw feeding back is provided with heater element.
Preferably, hot-air blower is arranged between adjacent two layers screw feeding plate, and hot-air blower quantity is no less than four.
This utility model has the advantage that and has the benefit effect that the pulverizing of crystal class and dry carries out simultaneously, process is more quick, operating procedure is simple, spiral transfer structure avoids the crystal powder after pulverizing to be bonded on dry tank wall, make the transmission that crystal powder is orderly, and increase drying efficiency, reduce wastage of material.
Accompanying drawing explanation
Fig. 1 is structural representation of the present utility model
In figure:
1, crush box 11, spiral smash axle group 12, dog-house
2, drying baker 21, center pillar 22, hot-air blower
23, screw feeding plate 3, transporter
Detailed description of the invention
Below in conjunction with accompanying drawing, an embodiment of the present utility model is explained.
As shown in Figure 1, this utility model relates to crystal continuous and pulverizes spiral drier, including crush box 1, drying baker 2 and transporter 3, crush box 1 is positioned at above drying baker 2, crush box 1 connects with drying baker 2, crush box 1 and drying baker 2 are cylindric casing, and crush box 1 is identical with drying baker 2 diameter, therefore crush box 1 and drying baker 2 are in integral type, crush box 1 top is provided with dog-house 12, it is provided with spiral in the middle part of crush box 1 and smashes axle group 11, axle is smashed including at least two spiral, drying baker 2 central authorities are provided with center pillar 21, center pillar 21 is around being provided with screw feeding plate 23, higher than inner side outside screw feeding plate 23, it is close-coupled on drying baker 2 sidewall outside screw feeding plate 23, such structure makes the crystal powder of pulverizing only by the downward landing of screw feeding plate 23, screw feeding plate 23 smooth surface, screw feeding plate 23 back side is provided with heater element, crystal powder is heated the state keeping dry in the process of landing, will not deliquescence or caking, it is not bound on screw feeding plate 23, hot-air blower 22 it is provided with inside drying baker 2, hot-air blower 22 is arranged between adjacent two layers screw feeding plate 23, hot-air blower 22 quantity is no less than four, hot-air blower 22 1 aspect plays the effect of heating aeration-drying, the downward landing of crystal powder can be promoted on the other hand, make crystal powder will not be deposited on screw feeding plate 23, therefore, two groups of hot-air blowers 22 it are provided with all vis-a-vis above every helical layer delivery sheet 23, hot-air blower 22 direction is downward along screw feeding plate 23, transporter 3 is arranged at below drying baker 2, screw feeding plate 23 end connects transporter 3, crystal powder is shifted by transporter 3 after prolonging screw feeding plate 23 landing, thus reaching the purpose worked continuously.
The work process of this example: crystal to be comminuted puts into crush box 1 by dog-house 12, smash axle group 22 through spiral and be broken into crystal powder, by the downward landing of screw feeding plate 23, screw feeding plate 23 back side is provided with heating element heater, crystal powder is made to be in isoperibol, avoid deliquescence caking phenomenon, under the wind-force effect of hot-air blower 22, fall in transporter 3 screw feeding plate 23.
Above an embodiment of the present utility model is described in detail, but described content has been only preferred embodiment of the present utility model, it is impossible to be considered for limiting practical range of the present utility model. All equalizations made according to this utility model application range change and improvement etc., all should still belong within patent covering scope of the present utility model.
Claims (3)
1. crystal continuous pulverizes spiral drier, it is characterized in that: include crush box, drying baker and transporter, described crush box is positioned at above described drying baker, described crush box connects with described drying baker, described crush box and described drying baker are cylindric casing, and described crush box is identical with described drying baker diameter, described crush box top is provided with dog-house, it is provided with spiral in the middle part of described crush box and smashes axle group, described drying baker central authorities are provided with center pillar, described center pillar is around being provided with screw feeding plate, higher than inner side outside described screw feeding plate, it is close-coupled at outside described screw feeding plate on described drying baker sidewall, it is provided with hot-air blower inside described drying baker, described transporter is arranged at below described drying baker, described screw feeding plate end connects described transporter.
2. crystal continuous according to claim 1 pulverizes spiral drier, it is characterised in that: described screw feeding plate smooth surface, described screw feeding back is provided with heater element.
3. crystal continuous according to claim 1 pulverizes spiral drier, it is characterised in that: described hot-air blower is arranged between adjacent two layers screw feeding plate, and described hot-air blower quantity is no less than four.
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201520962244.8U CN205308521U (en) | 2015-11-26 | 2015-11-26 | Spiral drying device is smashed in succession to crystal |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201520962244.8U CN205308521U (en) | 2015-11-26 | 2015-11-26 | Spiral drying device is smashed in succession to crystal |
Publications (1)
| Publication Number | Publication Date |
|---|---|
| CN205308521U true CN205308521U (en) | 2016-06-15 |
Family
ID=56189459
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| CN201520962244.8U Expired - Fee Related CN205308521U (en) | 2015-11-26 | 2015-11-26 | Spiral drying device is smashed in succession to crystal |
Country Status (1)
| Country | Link |
|---|---|
| CN (1) | CN205308521U (en) |
Cited By (3)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN109539699A (en) * | 2018-09-07 | 2019-03-29 | 北京化工大学 | A kind of cyclonic separation drier being separated by solid-liquid separation for water-containing granular materials |
| CN112728896A (en) * | 2020-12-28 | 2021-04-30 | 安徽丹泰仕机电设备有限公司 | Air current circulating type crushing dryer |
| CN114018029A (en) * | 2021-11-19 | 2022-02-08 | 遵义双河生物燃料科技有限公司 | Biofuel drying equipment |
-
2015
- 2015-11-26 CN CN201520962244.8U patent/CN205308521U/en not_active Expired - Fee Related
Cited By (4)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN109539699A (en) * | 2018-09-07 | 2019-03-29 | 北京化工大学 | A kind of cyclonic separation drier being separated by solid-liquid separation for water-containing granular materials |
| CN109539699B (en) * | 2018-09-07 | 2021-03-02 | 北京化工大学 | Cyclone separation dryer for solid-liquid separation of water-containing particle materials |
| CN112728896A (en) * | 2020-12-28 | 2021-04-30 | 安徽丹泰仕机电设备有限公司 | Air current circulating type crushing dryer |
| CN114018029A (en) * | 2021-11-19 | 2022-02-08 | 遵义双河生物燃料科技有限公司 | Biofuel drying equipment |
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Legal Events
| Date | Code | Title | Description |
|---|---|---|---|
| C14 | Grant of patent or utility model | ||
| GR01 | Patent grant | ||
| CF01 | Termination of patent right due to non-payment of annual fee | ||
| CF01 | Termination of patent right due to non-payment of annual fee |
Granted publication date: 20160615 Termination date: 20161126 |