Self-circulation drying and crushing mechanical mill
By using a self-circulating drying and pulverizing mechanical mill, the problem of the single function of existing equipment has been solved, realizing multi-functional processing of materials, improving drying and deagglomeration effects, and reducing production costs.
Patent Information
- Authority / Receiving Office
- CN · China
- Patent Type
- Utility models(China)
- Current Assignee / Owner
- Filing Date
- 2025-01-22
- Publication Date
- 2026-03-24
AI Technical Summary
Existing drying equipment has limited functionality and cannot simultaneously achieve material drying, deagglomeration, and classification. Furthermore, existing equipment is costly to manufacture and difficult to maintain, failing to meet diverse functional requirements.
A self-circulating drying and pulverizing mechanical mill is designed, including a honeycomb mill, a C-shaped tube, a first collector, and a second collector. Hot air and materials are conveyed by negative pressure to achieve drying, deagglomeration, and classification of materials. The system has a simple structure.
It improves the drying and deagglomeration effect of materials, realizes the graded treatment of materials, and has a simple overall structure and lower manufacturing cost.
Smart Images
Figure CN224025210U_ABST
Abstract
Description
TECHNICAL FIELD
[0001] The utility model belongs to material drying and grading equipment technical field, especially, relate to a self -circulation drying and crushing mechanical mill. BACKGROUND
[0002] In the drying equipment technical field, the similar equipment such as oven, belt dryer etc. on the current market has characteristics, but there is the problem of single function universally. They either only have drying function, or only have simple scattering ability, cannot realize multiple key functions simultaneously, seriously restrict the industry development and difficult to meet customer demand. For example, in many industries, the wet method superfine grinding material is easy to cake when drying, and the existing scattering machine is difficult to restore to the original particle size, which limits the application. Moreover, if the material surface modification is needed, the modification machine has to be added, and such equipment not only has high manufacturing cost, but also has great maintenance and operation difficulty, and the modification effect is not ideal. CONTENT OF THE UTILITY MODEL
[0003] To solve the technical problems of the prior art, the utility model provides a self -circulation drying and crushing mechanical mill, which can dry, depolymerize and grade the material, has good treatment effect, and the whole system structure is simple.
[0004] In order to realize the purpose of the utility model, the following scheme is adopted:
[0005] A self -circulation drying and crushing mechanical mill, comprising: honeycomb mill, C type pipe, first collector and second collector.
[0006] The honeycomb mill comprises a dispersion bin, a grinding bin and a sorting bin arranged in sequence from bottom to top and communicated with each other;
[0007] The sorting bin is internally provided with a grading impeller, the grading impeller divides the sorting bin into two sections, the first collector is communicated with the upper section of the sorting bin through a pipeline, the side wall of the lower section of the sorting bin is provided with a return pipe corresponding to the circumferential side of the grading impeller, the end of the return pipe extends to the outside of the sorting bin, and the return pipe is communicated with the C type pipe through a longitudinal pipeline;
[0008] The C type pipe is sleeved on the outer circumferential side of the dispersion bin;
[0009] One end of the C type pipe is provided with an air inlet pipe, and the air inlet pipe is communicated with a feeding pipe;
[0010] The other end of the C type pipe is provided with a three-way pipe, the other two ends of the three-way pipe are respectively communicated with the second collector and the dispersion bin, one end communicated with the second collector is provided with a control valve, one end communicated with the dispersion bin is provided with a second control valve, a secondary air hole is arranged on the pipeline between the second control valve and the dispersion bin, and the secondary air hole is provided with a valve;
[0011] The first collector and the second collector are both negative pressure collecting devices.
[0012] The utility model discloses beneficial effect lies in: this scheme can effectively improve the drying and depolymerization effect of material, and the classification processing of material is completed simultaneously, and the whole structure of system is simple, and the production cost is lower. BRIEF DESCRIPTION OF DRAWINGS
[0013] The drawings described herein are only for illustrating selected embodiments, not all possible implementation, and are not intended to limit the scope of the utility model.
[0014] Figure 1 The overall structure schematic diagram of the application is shown.
[0015] Figure 2 The structure and positional relation schematic diagram of honeycomb mill and C type pipe are shown.
[0016] Figure 3 The connection schematic diagram of honeycomb mill and first collector is shown.
[0017] Figure 4 The connection schematic diagram of honeycomb mill and second collector is shown.
[0018] Figure 5 The structure schematic diagram of wind wheel is shown.
[0019] Mark in the drawing: honeycomb mill-1, dispersion bin-11, grinding bin-12, sorting bin-13, back material pipe-131, longitudinal pipeline-132, classification impeller-14, rotating shaft-15, wind wheel-16, spiral plate-161, depolymerization wheel-17, C type pipe-2, air inlet pipe-21, feed pipe-22, first collector-3, second collector-4, three-way pipe-5, first control valve-51, second control valve-52, secondary air hole 53. DETAILED DESCRIPTION
[0020] In order to make the purpose, technical scheme and advantage of the utility model embodiment more clear, the embodiment of the utility model is explained in detail below in conjunction with the drawings, but the example described in the utility model is a part of the embodiment of the utility model, not all the embodiment.
[0021] As Figures 1 to 4 Shown, a kind of self-circulation dry crushing mechanical mill, including: honeycomb mill 1, C type pipe 2, first collector 3 and second collector 4.
[0022] Specifically, as Figure 2As shown, the honeycomb mill 1 includes a dispersion chamber 11, a grinding chamber 12 and a sorting chamber 13 arranged sequentially from bottom to top and interconnected. The dispersion chamber 11 is used to initially disperse the material entering the honeycomb mill 1, and the grinding chamber 12 can realize the functions of deagglomeration, crushing, shaping and modification of the material.
[0023] Specifically, such as Figures 1 to 4 As shown, the sorting chamber 13 is equipped with a grading impeller 14. As a conventional solution, the grading impeller 14 is directly driven by a motor, and the motor is located at the top of the sorting chamber 13 and the top of the honeycomb mill 1. The grading impeller 14 divides the sorting chamber 13 into upper and lower sections. The first collector 3 is connected to the upper section of the sorting chamber 13 through a pipe. The side wall of the lower section of the sorting chamber 13 is provided with a return pipe 131 corresponding to the periphery of the grading impeller 14. The end of the return pipe 131 extends to the outside of the sorting chamber 13 and is connected to the C-shaped pipe 2 through a longitudinal pipe 132.
[0024] Specifically, in combination Figures 1 to 3 As shown, the C-shaped tube 2 is fitted onto the outer periphery of the dispersion chamber 11.
[0025] Specifically, in combination Figures 1 to 3 As shown, one end of the C-shaped tube 2 is provided with an air inlet pipe 21, and the air inlet pipe 21 is connected to a feed pipe 22.
[0026] Specifically, such as Figure 1 As shown, the other end of the C-shaped pipe 2 is provided with a three-way pipe 5. The other two ends of the three-way pipe 5 are respectively connected to the second collector 4 and the dispersion chamber 11. The end connected to the second collector 4 is provided with a first control valve 51, and the end of the three-way pipe 5 connected to the dispersion chamber 11 is provided with a second control valve 52. The pipe between the second control valve 52 and the dispersion chamber 11 is provided with a secondary air hole 53, and the secondary air hole 53 is provided with a valve.
[0027] Both the first collector 3 and the second collector 4 are negative pressure collection devices. Specifically, both the first collector 3 and the second collector 4 are dust collectors.
[0028] There are two main working modes during production: one is crushing and deagglomeration, and the other is shaping.
[0029] like Figures 1 to 3As shown, during the crushing and depolymerization, the first control valve 51 is closed, and the first collector 3 is started, which generates negative pressure inside the honeycomb mill 1, and the hot air enters the inlet pipe 21 through the negative pressure conveying, and the material raw material is put into the inlet pipe 21 at the same time. Specifically, the temperature of the hot air is 200-500°C. The material and the hot air enter the C-shaped pipe 2 at the same time after mixing in the inlet pipe 21, and the material can be preheated by the hot air in this process; the mixed material and the hot air finally enter the dispersion bin 11 from the three-way pipe 5, and the material is preliminarily dispersed in the dispersion bin 11. The dispersed material automatically rises to the grinding bin 12 along with the negative pressure airflow, and the grinding bin 12 performs powder grinding, depolymerization and shaping treatment on the entering material. The surface modification of the material can also be realized by adding the modifier in this process. The processed material enters the lower section of the sorting bin 13, and finally the small-particle-size material enters the inside of the classification impeller 14 through the gap between the blades of the classification impeller 14, and smoothly enters the upper section of the sorting bin 13, and then smoothly enters the inside of the first collector 3 through the pipeline to achieve the purpose of collecting small-particle-size material. During the classification of the material by the classification impeller 14, under the action of the centrifugal force generated by the rotation of the classification impeller, the large-particle-size material cannot enter the inside of the classification impeller and is cut tangentially to enter the return pipe 131, and then flows back to the C-shaped pipe 2 through the longitudinal pipeline 132, and finally enters the dispersion bin 11, the grinding bin 12 and the sorting bin 13 again for cyclic crushing and classification treatment, until the material raw material is processed or the raw material is stopped. In the process of multiple cycles, the material is continuously contacted with the hot air, so that the drying effect of the material is better.
[0030] As shown in Figure 1 , Figure 2 and Figure 4 , during the shaping, the first control valve 51 is closed, the valve of the secondary air hole 53 is closed, the second control valve 52 is opened, and the shaped material enters the grinding bin 12 for cyclic shaping. After the shaping is completed, the feeding is stopped, the first control valve 51 is opened, the valve of the secondary air hole 53 is opened, and the second control valve 52 is closed. The shaped material enters the second collector 4 for finished product collection, and the debris in the shaping process is collected by the first collector 3.
[0031] The above processing method can realize the cyclic crushing, depolymerization and shaping of the material, and the overall structure of the system is simple and the manufacturing cost is lower.
[0032] Preferably, as shown in Figure 2As shown in the drawings, the bottom of the honeycomb mill 1 is provided with a rotating shaft 15, the upper section of the rotating shaft 15 extends into the dispersion bin 11 and the grinding bin 12, the rotating shaft 15 is coaxially provided with at least one wind wheel 16, the wind wheel 16 is located inside the dispersion bin 11 and is used for dispersing the material, the upper end of the rotating shaft 15 is provided with a depolymerization wheel 17, the depolymerization wheel 17 is located inside the grinding bin 12 and is used for depolymerizing the material, and the rotating shaft 15 is driven by a motor; as a preferred scheme, the motor driving the rotating shaft 15 is arranged at the bottom of the honeycomb mill 1, and the motor and the lower end of the rotating shaft 15 are connected through a belt drive.
[0033] Preferably, the depolymerization wheel 17 comprises an upper and lower support assembly and a disc, the support assembly is welded to the rotating shaft 15 and is used for forming a frame structure of the depolymerization wheel 17, and the disc is connected to the support assembly through a clamping groove; as a preferred scheme, the tangential angle between the disc and the support assembly is adjustable, so that the material can be crushed, depolymerized, shaped, dried, modified and the like.
[0034] Preferably, as shown in the drawings, Figure 5 Preferably, the wind wheel 16 is a circular ring plate structure, the bottom surface of the wind wheel 16 is provided with a plurality of spiral plates 161 along the circumference, and the wind wheel 16 is rotated by the rotating shaft 15 during work, so that the material can be dispersed by the spiral plates 161, and the spiral plates 161 form an inner vortex, the inner vortex makes the dispersed material more smoothly enter the grinding bin 12, and the flow field distribution of the airflow is more uniform, which helps to improve the dispersion efficiency and prevent the material from accumulating in a local part.
[0035] Preferably, as shown in the drawings, Figure 1 Preferably, the plurality of return material pipes 131 are arranged along the circumference of the sorting bin 13, and the end of each return material pipe 131 is provided with a longitudinal pipeline 132 in communication with the C-shaped pipe 2, so as to improve the efficiency of collecting the large-particle-diameter material in reflux.
[0036] Preferably, as shown in the drawings, Figure 1 Preferably, the return material pipe 131 is arranged along the tangent direction of the sorting bin 13, and the end is directed in the same direction as the rotating direction of the grading impeller 14, so as to further improve the efficiency of the large-particle-diameter material in reflux.
[0037] The above only describes the preferred embodiments of the present application, and does not mean that it is the only or limiting the present application. Those skilled in the art should understand that various changes or equivalent replacements made to the present application without departing from the scope of the present application, all belong to the scope of protection of the present application.
Claims
1. A self-circulating dry pulverizing mechanical mill characterized by, The utility model relates to a kind of honeycomb mill, including: honeycomb mill (1), C type pipe (2), first collector (3) and second collector (4); Honeycomb mill (1) includes dispersion bin (11), grinding bin (12) and sorting bin (13) sequentially arranged from bottom to top and communicated with each other; Sorting bin (13) is provided with grading impeller (14) inside, grading impeller (14) divides sorting bin (13) into two sections, first collector (3) is communicated with the upper section of sorting bin (13) by pipeline, the lateral wall of the lower section of sorting bin (13) is provided with return pipe (131) corresponding to the circumferential side of grading impeller (14), the end of return pipe (131) extends to the outside of sorting bin (13), and is communicated with C type pipe (2) by a longitudinal pipeline (132); C type pipe (2) is sleeved on the circumferential side of dispersion bin (11); One end of C type pipe (2) is provided with air inlet pipe (21), and air inlet pipe (21) is provided with feed pipe (22) in communication; The other end of C type pipe (2) is provided with three-way pipe (5), the other two ends of three-way pipe (5) are respectively communicated with second collector (4) and dispersion bin (11), and one end communicated with second collector (4) is provided with first control valve (51), one end of three-way pipe (5) communicated with dispersion bin (11) is provided with second control valve (52), and secondary air hole (53) is provided on the pipeline between second control valve (52) and dispersion bin (11), and secondary air hole (53) is provided with valve. First collector (3) and second collector (4) are both negative pressure collection devices. First collector (3) and second collector (4) are both dust collectors.
2. A self-circulating dry pulverizing mechanical mill according to claim 1, characterized in that, Honeycomb mill (1) is provided with rotating shaft (15) at the bottom, the upper section of rotating shaft (15) extends into dispersion bin (11) and grinding bin (12), rotating shaft (15) is coaxially provided with at least one wind wheel (16), wind wheel (16) is located in dispersion bin (11), the upper end of rotating shaft (15) is provided with depolymerization wheel (17), depolymerization wheel (17) is located in grinding bin (12), and rotating shaft (15) is driven by motor.
3. A self-circulating dry pulverizing mechanical mill according to claim 1, characterized in that, Depolymerization wheel (17) includes upper and lower support assemblies and a disc, the support assemblies are welded to rotating shaft (15), and the disc is connected to the support assemblies by a clamping groove.
4. A self-circulating dry pulverizing mechanical mill according to claim 3, wherein, Wind wheel (16) is a circular plate structure, and a plurality of spiral plates (161) are arranged in an array on the bottom surface along the circumference.
5. A self-circulating dry pulverizing mechanical mill according to claim 3, wherein, A plurality of return pipes (131) are arranged in an array along the circumference of sorting bin (13), and the end of each return pipe (131) is provided with a longitudinal pipeline (132) communicated with C type pipe (2).
6. A self-circulating dry pulverizing mechanical mill according to claim 1, wherein, Return pipe (131) is arranged along the tangent direction of sorting bin (13), and the end is directed in the same direction as the rotation direction of grading impeller (14).
7. A self-circulating dry pulverizing mechanical mill according to claim 1 or 6, characterized in that,