CN201720956U - Macromoleclar polymer colloid cyclone granulator - Google Patents
Macromoleclar polymer colloid cyclone granulator Download PDFInfo
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- CN201720956U CN201720956U CN2010202069723U CN201020206972U CN201720956U CN 201720956 U CN201720956 U CN 201720956U CN 2010202069723 U CN2010202069723 U CN 2010202069723U CN 201020206972 U CN201020206972 U CN 201020206972U CN 201720956 U CN201720956 U CN 201720956U
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- whirlwind
- granulation
- discharging opening
- colloid
- polymer colloid
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Abstract
The utility model discloses a macromoleclar polymer colloid cyclone granulator, which comprises a motor, a machine body sleeve, a charging opening and a discharging opening. A plurality of sets of cyclone blades and sieving trays are sequentially arranged along the vertical direction of the motor spindle between the charging opening and the discharging opening. The sieving trays are provided with through holes for granules through. Colloids are cut and crushed by the multistage cyclone blades which can axially rotate at high speed, so as to achieve the granulating effect. With compact structure, high stability and convenient field installation, the complete machine reduces speed without a speed reducer. When in granulation, secondary extrusion to the colloid does not exist and the inherent attribute of the colloid is unchanged. Filtering is performed by a multistage sieving plate to meet the granulation process of granules with different granule diameters and widen the granulation range. The complete machine has high efficient and cannot be easily blocked, thereby meeting the granulation manufacturing demand of colloidal macromoleclar polymer similar to polyacrylamide.
Description
Technical field
The utility model relates to a kind of prilling granulator, and especially a kind of polypropylene-like acid amides etc. of realizing has the device of high viscosity, the granulation of high resiliency polymeric colloid.
Background technology
The gluey high molecular polymer of polypropylene-like acid amides, moisture height has stronger viscoplasticity, and manufacturer needs post processing aborning, and removing wherein, moisture carries out drying; But, blob of viscose convection drying to large volume is very difficult, the energy consumption height, efficient is low, and the large volume blob of viscose must be cut apart fragmentation in the production becomes granule, improves the specific area of material, to improve its drying efficiency, if the grain graininess that generates in the production is more little, then material specific surface area is big more, and the easy more drying of carrying out is handled.So the polyacrylamide post processing focus on granulation, granulation smoothly whether, directly have influence on the subsequent drying process.At present, the comminutor that enterprise uses, principle all is to utilize screw rod or other form chargings basically, mesh is extruded, the method granulation that cutting knife cuts off.A kind of polyacrylamide colloid comminutor as Chinese patent specification CN 2383652Y discloses; this machine is adorned the barrel of making that has a plurality of through holes on a bottom and the periphery in the screw extruder lower end, thereby the double helix bar that has a vertical cutting knife of the wheeled multiple-cutting-edge of columnar tooth is delivered to the colloid material to make in the barrel and extrude and cut off by through hole and formed particle.This structure wants first extruded material to cut into particle again, colloid in use often takes place stop up, and causes the granulation obstacle, has to shut down and tears the machine cleaning open, causes the increase of workload, and production cost improves, decrease in efficiency; Extruding during granulation may destroy the colloid institutional framework; The comminutor of this type adopts the screw rod pusher simultaneously, must add decelerator, and the comminutor equipment volume is big, and the production cost height is installed and used inconvenience.
The utility model content
The purpose of this utility model provides a kind of simple in structure, and compact conformation is applicable to that polypropylene-like acid amides etc. has the prilling granulator of high viscosity, high resiliency polymer, can well solve the problem of above-mentioned existence.
The purpose of this utility model is to be achieved through the following technical solutions:
A kind of high molecular polymer colloid whirlwind comminutor; comprise motor, fuselage sleeve, charging aperture and discharging opening; along electric machine main shaft many group whirlwind blades and screen tray are installed successively vertically between described charging aperture and discharging opening, described screen tray has the open-work that passes through for pellet.
Further, the physical dimension of described open-work is from up to down dwindled successively with screen tray.
Further, described whirlwind blade has the blade that a plurality of bendings are tiltedly opened.
Further, described discharging opening is positioned at the sidewall of fuselage lower cartridge, and corresponding discharging opening is equipped with on electric machine main shaft and gets rid of the material awl.
Further, described fuselage sleeve is divided into multistage granulation chamber by a plurality of screen traies, all comprises a whirlwind blade in every grade of granulation chamber.
Simultaneously, for reaching better control and energy-saving effect, described motor adopts the VFC motor.
The utility model provides a kind of whirlwind comminutor of brand new, and the multistage cyclone blade that adopts axial high speed to rotate carries out cutting and crushing to colloid and reaches the granulation effect, and complete machine slows down without reductor, compact conformation, and stability is high, and is on-the-spot easy for installation; Granulation process does not produce secondary extrusion to colloid, does not change the intrinsic attribute of colloid; Adopt multistage sieve plate to filter, can satisfy the granulation process of different-grain diameter, the granulation wide ranges; The overall efficiency height is not easy blockage phenomenon, can satisfy the granulation production of the gluey high molecular polymer of polypropylene-like acid amides.
Description of drawings
With embodiment the utility model is described in further detail with reference to the accompanying drawings below.
Fig. 1 is the structural representation of whirlwind comminutor described in the utility model.
Fig. 2 is the front view of described whirlwind comminutor screen tray
Fig. 3 is the front view of described whirlwind granulator blade
Fig. 4 is the vertical view of the described whirlwind granulator blade of Fig. 3.
Among the figure:
1, charging aperture; 2, main shaft; 3, whirlwind blade; 4, screen tray; 5, fuselage sleeve; 6, get rid of the material awl; 7, motor; 8, one-level granulation chamber; 9, secondary granulation chamber; 10, three grades of granulation chambeies; 11, level Four granulation chamber; 12, discharging chamber; 13, frame; 14, open-work; 15, bending tiltedly edges a knife.
The specific embodiment
Shown in Fig. 1 to 4, provided the structural representation of a specific embodiment of the present utility model, as shown in the figure, complete machine comprises motor 7, fuselage sleeve 5, charging aperture 1 and the discharging opening of vertical installation, the last termination colloid of charging aperture 1 is made the discharging opening of reactor, along electric machine main shaft 2 many group whirlwind blades 3 and screen tray 4 are installed successively vertically between described charging aperture 1 and discharging opening, described screen tray 4 has the open-work 14 that passes through for pellet, as shown in Figure 2.
The physical dimension of open-work 14 is from up to down dwindled successively with screen tray 4, and described screen tray 4 can replace with similar structure, size, shape and the quantity of the open-work 14 of screen tray can with pellet pass through require to change.
During production, material with lower pressure in charging aperture 1 enters one-level granulation chamber 8, electric machine main shaft 2 drives 3 pairs of colloids of whirlwind blade and carries out cutting and crushing, the colloidal solid that granularity is little is under the effect of whirlwind cutter simultaneously, produce axially-movable, enter secondary granulation chamber 9 by the open-work on the screen tray 4 14, in secondary granulation chamber 9, whirlwind blade 3 cutting and crushings that colloidal solid further is rotated, granularity continues to diminish, cut through the echelon in three grades of granulation chambeies 10 and level Four granulation chamber 11 more successively, the end product particle enters the discharging chamber 12 that is positioned at the fuselage lower cartridge by screen tray 4, and its sidewall is provided with discharging opening, and corresponding discharging opening is equipped with on electric machine main shaft and gets rid of material awl 6, pellet is rotated gets rid of material awl 6 and throws away from discharging opening, finishes the material process of making.
Adopt the stepless time adjustment motor to replace common motor conveniently to control, regulate the rotary speed of blade, reach better energy-saving effect simultaneously.
Above-mentioned explanation is specifying at the feasible embodiment of the utility model; and this embodiment is not in order to limit claim of the present utility model; allly do not break away from the equivalence that the utility model technical spirit done and implement or change, the embodiment that for example adopt difform blade, has a sieve plate of difformity open-work all should be contained in the claimed claim of the application.
Claims (6)
1. high molecular polymer colloid whirlwind comminutor; comprise motor, fuselage sleeve, charging aperture and discharging opening; it is characterized in that: along electric machine main shaft many group whirlwind blades and screen tray are installed successively vertically between described charging aperture and discharging opening, described screen tray has the open-work that passes through for pellet.
2. high molecular polymer colloid whirlwind comminutor according to claim 1, it is characterized in that: the physical dimension of described open-work is from up to down dwindled successively with screen tray.
3. high molecular polymer colloid whirlwind comminutor according to claim 1 is characterized in that: described whirlwind blade has the blade that a plurality of bendings are tiltedly opened.
4. high molecular polymer colloid whirlwind comminutor according to claim 1, it is characterized in that: described discharging opening is positioned at the sidewall of fuselage lower cartridge, and corresponding discharging opening is equipped with on electric machine main shaft and gets rid of the material awl.
5. according to the described a kind of high molecular polymer colloid whirlwind comminutor of arbitrary claim in the claim 1 to 4, it is characterized in that: described fuselage sleeve is divided into multistage granulation chamber by a plurality of screen traies, all comprises a whirlwind blade in every grade of granulation chamber.
6. a kind of high molecular polymer colloid whirlwind comminutor according to claim 5 is characterized in that: described motor adopts the VFC motor.
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN2010202069723U CN201720956U (en) | 2010-05-28 | 2010-05-28 | Macromoleclar polymer colloid cyclone granulator |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN2010202069723U CN201720956U (en) | 2010-05-28 | 2010-05-28 | Macromoleclar polymer colloid cyclone granulator |
Publications (1)
| Publication Number | Publication Date |
|---|---|
| CN201720956U true CN201720956U (en) | 2011-01-26 |
Family
ID=43489244
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| CN2010202069723U Expired - Fee Related CN201720956U (en) | 2010-05-28 | 2010-05-28 | Macromoleclar polymer colloid cyclone granulator |
Country Status (1)
| Country | Link |
|---|---|
| CN (1) | CN201720956U (en) |
Cited By (2)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN102126264A (en) * | 2011-02-22 | 2011-07-20 | 深圳市宜和勤环保科技有限公司 | Micro crusher with inner and outer barrels |
| CN114768677A (en) * | 2022-06-24 | 2022-07-22 | 山东百农思达生物科技有限公司 | Prilling granulator is used in germicide preparation |
-
2010
- 2010-05-28 CN CN2010202069723U patent/CN201720956U/en not_active Expired - Fee Related
Cited By (4)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN102126264A (en) * | 2011-02-22 | 2011-07-20 | 深圳市宜和勤环保科技有限公司 | Micro crusher with inner and outer barrels |
| CN102126264B (en) * | 2011-02-22 | 2013-04-24 | 深圳市宜和勤环保科技有限公司 | Micro crusher with inner and outer barrels |
| CN114768677A (en) * | 2022-06-24 | 2022-07-22 | 山东百农思达生物科技有限公司 | Prilling granulator is used in germicide preparation |
| CN114768677B (en) * | 2022-06-24 | 2022-08-23 | 山东百农思达生物科技有限公司 | Prilling granulator is used in germicide preparation |
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Legal Events
| Date | Code | Title | Description |
|---|---|---|---|
| C14 | Grant of patent or utility model | ||
| GR01 | Patent grant | ||
| C17 | Cessation of patent right | ||
| CF01 | Termination of patent right due to non-payment of annual fee |
Granted publication date: 20110126 Termination date: 20130528 |