CN203803599U - Stearate pulverizing device - Google Patents
Stearate pulverizing device Download PDFInfo
- Publication number
- CN203803599U CN203803599U CN201420042431.XU CN201420042431U CN203803599U CN 203803599 U CN203803599 U CN 203803599U CN 201420042431 U CN201420042431 U CN 201420042431U CN 203803599 U CN203803599 U CN 203803599U
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- CN
- China
- Prior art keywords
- pulverizer
- stearate
- thin material
- cyclone dust
- air
- 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 discloses a stearate pulverizing device. The stearate pulverizing device is characterized by comprising a pulverizer, a first cyclone dust extractor, a first intermediate storage bin, a first airflow vortex pulverizer, a second cyclone dust extractor, a first end product storage bin, a first bag-type dust remover, a second intermediate storage bin, a second airflow vortex pulverizer, a second bag-type dust remover and a second end product storage bin, wherein the pulverizer comprises a housing, a fine material screen mesh, a fine material storage bin and pulverizing blades; the fine material screen mesh in the housing divides the pulverizer into a material pulverizing cavity and a fine material storage cavity; materials in both the material pulverizing cavity and the fine material storage cavity are subjected to secondary pulverizing and dusting to obtain the end product. The stearate pulverizing device has a simple structure and can utilize one piece of equipment to produce stearate of different specifications, thereby achieving low equipment investment.
Description
Technical field
The utility model relates to a kind of hard hydrochlorate process equipment, is specifically related to a kind of stearate reducing mechanism, belongs to technical field of chemical.
Background technology
Stearate is one of principal item of polyvinyl chloride (PVC) processing aid, and it can be used as heat stabilizer and the lubricant of PVC, is widely used in various soft and hard products.Different industries requires different for the particle diameter of stearate, for example: it is that 200 orders can meet the demands that plastic industry requires the particle diameter of stearate, and rubber industry for the particle diameter of stearate, to require be 325 orders.In order to meet the demand of user to stearate different-grain diameter, stearate manufacturing enterprise normally adopts many complete equipments to produce the product of different size or uses the product of same set of device fabrication different-grain diameter, the product that uses many complete equipments to produce different size exists equipment investment to increase, the defect that production cost is high, adopt the product of same device fabrication different-grain diameter owing to there being feeding capacity and the isoparametric process of rotating speed that needs parking to adjust pulverizer, therefore easily affect production efficiency, if and do not stopped, the product of the producing use of can only demoting, cause the waste of product.
Utility model content
It is even that the technical problems to be solved in the utility model is to provide a kind of material, can produce the stearate reducing mechanism of different size particle simultaneously.
For solving the problems of the technologies described above, the technical solution adopted in the utility model is: the continuous reducing mechanism of a kind of stearate, and its innovative point is: comprise pulverizer, the first cyclone dust collectors, the first intermediate bunker, the first air-flow vortex pulverizer, the second cyclone dust collectors, the first finished product bin, the first sack cleaner, the second intermediate bunker, the second air-flow vortex pulverizer, the second sack cleaner, the second finished product bin;
Described pulverizer comprises shell, thin material screen cloth, thin material storage silo and Disintegrating knife; Described enclosure arranges the thin material screen cloth of one deck, and described thin material screen cloth arranges with shell is concentric, and pulverizer is divided into crushing material chamber and thin material storage chamber; Described crushing material arranges Disintegrating knife in chamber, and Disintegrating knife is driven by motor, and crushing chamber is connected with the first cyclone dust collectors by valve; Described the first cyclone dust collectors connect the first intermediate bunker, and the first intermediate bunker connects the first air-flow vortex pulverizer; Described the first air-flow vortex pulverizer connects the second cyclone dust collectors, and the second cyclone dust collectors connect the first finished product bin; One row's material pilot hole is set on described disintegrator shell, and disintegrator shell is by pilot hole and thin material storage silo UNICOM, and described thin material storage silo is connected with the first sack cleaner by valve; Described the first bag dust device connects the second intermediate bunker, and the second intermediate bunker connects the second air-flow vortex pulverizer; Described the second air-flow vortex pulverizer connects the second sack cleaner, and the second sack cleaner connects the second finished product bin.
Further, described screen cloth is 160～200 object stainless steel mesh.
The beneficial effects of the utility model: by a thin material screen cloth is set in casing inside, stearate after pulverizing enters respectively the crushing chamber in thin material storage chamber, thin material storage chamber obtains into this product through the broken machine of reground grain respectively with the material of different-grain diameter in crushing chamber after deduster, the utility model is simple in structure, the stearate that can utilize same device fabrication different size, equipment investment is few.
Accompanying drawing explanation
Fig. 1 is structural representation of the present utility model.
The specific embodiment
Below in conjunction with the drawings and specific embodiments, the technical solution of the utility model is elaborated.
The continuous reducing mechanism of a kind of stearate as shown in Figure 1, comprises pulverizer 1, the first cyclone dust collectors 2, the first intermediate bunker 3, the first air-flow vortex pulverizer 4, the second cyclone dust collectors 5, the first finished product bin 6, the first sack cleaner 7, the second intermediate bunker 8, the second air-flow vortex pulverizer 9, the second sack cleaner 10, the second finished product bin 11.
Pulverizer 1 comprises shell 01, thin material screen cloth 02, thin material storage silo 03 and Disintegrating knife 04, and wherein thin material screen cloth 02 is 160～200 object stainless steel mesh; Shell 01 inside arranges the thin material screen cloth 02 of one deck, and thin material screen cloth 02 and the concentric setting of shell 01 are divided into crushing material chamber and thin material storage chamber by pulverizer 1; Disintegrating knife 04 is set in crushing material chamber, Disintegrating knife 04 is driven by motor, stearate is in the pulverizing of crushing material chamber process Disintegrating knife 04, centrifugal action at pulverizer is little, the stearate of fine particle enters thin material storage silo 03 by thin material screen cloth 02, and the stearate that particle diameter is larger is stayed in crushing chamber.
Crushing chamber is connected 2 by valve with the first cyclone dust collectors; The first cyclone dust collectors 2 connect the first intermediate bunker 3, the first intermediate bunker 3 connects the first air-flow vortex pulverizer 4, the first air-flow vortex pulverizer 4 connects the second cyclone dust collectors 5, the second cyclone dust collectors 5 connect the first finished product bin 6, and the large-size particles stearate in crushing chamber obtains large particle diameter stearate finished product after again pulverizing processing and dedusting.
One row's material pilot hole 05 is set on disintegrator shell 01, and disintegrator shell 01 is by pilot hole 05 and thin material storage silo 03 UNICOM, and thin material storage silo 03 is connected with the first sack cleaner 7 by valve; The first bag dust device 7 connects the second intermediate bunker 8, the second intermediate bunkers 8 and connects the second air-flow vortex pulverizer 9; The second air-flow vortex pulverizer 9 connects the second sack cleaner 10, the second sack cleaners 10 and connects the second finished product bin 11, and the small size particle stearate in thin material storage silo 03 obtains small particle diameter stearate finished product after again pulverizing processing and dedusting.
Claims (2)
1. a stearate reducing mechanism, is characterized in that: comprise pulverizer, the first cyclone dust collectors, the first intermediate bunker, the first air-flow vortex pulverizer, the second cyclone dust collectors, the first finished product bin, the first sack cleaner, the second intermediate bunker, the second air-flow vortex pulverizer, the second sack cleaner, the second finished product bin;
Described pulverizer comprises shell, thin material screen cloth, thin material storage silo and Disintegrating knife; Described enclosure arranges the thin material screen cloth of one deck, and described thin material screen cloth arranges with shell is concentric, and pulverizer is divided into crushing material chamber and thin material storage chamber; Described crushing material arranges Disintegrating knife in chamber, and Disintegrating knife is driven by motor, and crushing chamber is connected with the first cyclone dust collectors by valve; Described the first cyclone dust collectors connect the first intermediate bunker, and the first intermediate bunker connects the first air-flow vortex pulverizer; Described the first air-flow vortex pulverizer connects the second cyclone dust collectors, and the second cyclone dust collectors connect the first finished product bin; One row's material pilot hole is set on described disintegrator shell, and disintegrator shell is by pilot hole and thin material storage silo UNICOM, and described thin material storage silo is connected with the first sack cleaner by valve; Described the first bag dust device connects the second intermediate bunker, and the second intermediate bunker connects the second air-flow vortex pulverizer; Described the second air-flow vortex pulverizer connects the second sack cleaner, and the second sack cleaner connects the second finished product bin.
2. a kind of stearate reducing mechanism according to claim 1, is characterized in that: described screen cloth is 160～200 object stainless steel mesh.
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201420042431.XU CN203803599U (en) | 2014-01-23 | 2014-01-23 | Stearate pulverizing device |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201420042431.XU CN203803599U (en) | 2014-01-23 | 2014-01-23 | Stearate pulverizing device |
Publications (1)
| Publication Number | Publication Date |
|---|---|
| CN203803599U true CN203803599U (en) | 2014-09-03 |
Family
ID=51442410
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| CN201420042431.XU Expired - Fee Related CN203803599U (en) | 2014-01-23 | 2014-01-23 | Stearate pulverizing device |
Country Status (1)
| Country | Link |
|---|---|
| CN (1) | CN203803599U (en) |
Cited By (1)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN106423486A (en) * | 2016-11-10 | 2017-02-22 | 佛山市利德嘉陶瓷制釉有限公司 | Multi-split fluidized bed airflow mill |
-
2014
- 2014-01-23 CN CN201420042431.XU patent/CN203803599U/en not_active Expired - Fee Related
Cited By (1)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN106423486A (en) * | 2016-11-10 | 2017-02-22 | 佛山市利德嘉陶瓷制釉有限公司 | Multi-split fluidized bed airflow mill |
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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: 20140903 Termination date: 20180123 |