Uniform mixing and stirring device for micron-sized photovoltaic glass powder
By setting a grading tank and a centrifugal component in the stirring device and using a power component and a blower to achieve airflow grading and automatic transportation, the problem of mixing uniformity of micron-level photovoltaic glass powder is solved, the grading efficiency and degree of automation are improved, and the equipment cost is reduced.
Patent Information
- Application Number
- CN202511300413.6
- Authority / Receiving Office
- CN · China
- Patent Type
- Applications(China)
- Current Assignee / Owner
- Filing Date
- 2025-09-12
- Publication Date
- 2025-10-17
- Estimated Expiration
- Not applicable · inactive patent
AI Technical Summary
Existing technologies make it difficult to achieve uniform mixing of micron-sized photovoltaic glass powder. Traditional crushing equipment is difficult to mix evenly, the airflow classification accuracy is limited, the degree of automation is low, the equipment cost is high, and continuous processing cannot be achieved.
A grading tank and a centrifugal assembly are set in the stirring device. The centrifugal assembly is driven to rotate by the power assembly, and the air flow classification is achieved in conjunction with the blower. Large and small particles are automatically transported during the rotation process, simplifying the material preparation process.
It realizes the continuous and uninterrupted feeding and uniform stirring processing of micron-level photovoltaic glass powder, improves the grading efficiency and degree of automation, and reduces equipment costs and space occupancy.
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Figure CN120789971A_ABST
Abstract
Description
TECHNICAL FIELD
[0001] The present application relates to the field of stirring dispersion technology, in particular to a mixing and uniform stirring device for micron-level photovoltaic glass powder. BACKGROUND
[0002] In many industries such as chemical industry, pharmaceutical industry, and material industry, there is an increasing demand for ultra-fine powders with specific particle size distribution. Ultra-fine powders with different particle size ratios can endow products with different physical and chemical properties, meeting the diverse application requirements. Among them, glass powder is a micron-level powder made of inorganic glass through crushing, grinding, and grading, and its main components are silicon dioxide (SiO2) and boron oxide (B2O3). Depending on the purpose, metal oxides can be added to adjust the performance. For example, cobalt and chromium pigments can be added for decorative purposes.
[0003] Currently, the processing of ultra-fine materials usually adopts the method of crushing first and then mixing, but there are many shortcomings. Traditional crushing equipment often cannot mix the materials uniformly, leading to increased difficulty in subsequent grading; the grading precision of air flow grading system is limited, and it cannot accurately separate powders of different particle sizes; the degree of automation is low, and it is difficult to achieve accurate proportioning of powders of different particle sizes, and errors may occur during the proportioning process.
[0004] On the other hand, the mixing and uniform stirring device for micron-level photovoltaic glass powder in the existing scheme needs to use multiple processes such as grading, quantitative proportioning, conveying, and stirring, resulting in a large number of equipment requirements, large space occupation, high equipment cost, and the grading process is easily disturbed by the falling point of raw materials, and the processing process needs to be put in batches, which cannot realize continuous feeding and processing. SUMMARY
[0005] To solve the problems in the background art, the present application provides a mixing and uniform stirring device for micron-level photovoltaic glass powder. The device is provided with a grading tank at the top, and a centrifugal component is directly driven to rotate by a power assembly. The air flow grading process of the feeding raw materials can be realized by cooperating with the air blower at the bottom. During the rotation process, the large and small size particles after grading are automatically transported towards the bottom, so as to achieve continuous and uninterrupted feeding and discharging and uniform stirring processing, simplifying the preparation process.
[0006] In order to achieve the above object, the application is realized by the following technical scheme: a kind of mixing uniform stirring device of micron photovoltaic glass powder, including stirring device body, the stirring device body includes stirring tank, grading tank, centrifugal component and power component, the inside of the stirring tank is inserted with stirring shaft, the side of the stirring shaft is equipped with stirring rod, and the top of stirring shaft is equipped with bearing, the top of the stirring tank is welded with quantitative channel, the top of the quantitative channel is welded with grading tank, the inside of the grading tank is equipped with centrifugal component, the side of the stirring tank is integrally formed with extension plate, the top of the extension plate is welded with stand, the top of the stand is welded with support plate, the end of the support plate is built with power component, the bottom of the centrifugal component is embedded with ball, and centrifugal component is pressed in the inside of grading tank by ball, the middle area below the centrifugal component is provided with transmission mechanism, the end of the transmission mechanism is inserted into the inside of quantitative channel, and transmission mechanism and quantitative channel are installed on the both sides of the bottom of grading tank in symmetrical form.
[0007] Further, the centrifugal component includes centrifugal bin, top layer butt joint sleeve and bottom layer butt joint sleeve, the top layer butt joint sleeve is integrally formed at the top of the centrifugal bin, the bottom of the centrifugal bin is integrally formed with the bottom layer butt joint sleeve, and the bottom of the both ends of the centrifugal bin is provided with movable butt joint hole.
[0008] Further, the power component includes motor, driving shaft, driving gear and driven gear, the motor is screwed on the surface of the support plate, the output end of the motor is connected with the driving shaft, and the end of the driving shaft is keyed with the driving gear.
[0009] Further, the surface of the top layer butt joint sleeve is welded with the driven gear, the driving gear and the driven gear are engaged, the top layer butt joint sleeve is inserted with injection channel above, the injection channel is used to transport the raw material after photovoltaic glass powder crushing to the inside of the centrifugal component, the inner wall top of the centrifugal bin is installed with diffusion pipeline, and the middle of the diffusion pipeline is communicated with the inside of the top layer butt joint sleeve.
[0010] Further, the grading tank includes supporting plate, fitting plate and grading bin, the fitting plate is arranged on the inside of the grading tank, the both ends of the fitting plate are provided with grading bin, and the inner wall of each grading bin is provided with fixed butt joint hole.
[0011] Further, the bottom of the grading tank is integrally formed with the supporting plate, the centrifugal component is pressed on the supporting plate by the ball of bottom, and the end of the centrifugal bin is used to press on the surface of the fitting plate, and the middle area of the top and bottom of the grading tank is in open state.
[0012] Further, the grading tank is fixed as a whole with the lower stirring tank through the quantitative channel, the grading bin is arranged in a symmetrical form on the two sides of the grading tank, and gaps are arranged between the two ends of the centrifugal bin and the inner wall top end of the grading tank.
[0013] Further, the transmission mechanism comprises a driven shaft, a blocking column, a first bevel gear and a second bevel gear, the surface of the bottom butt joint sleeve is key-connected with the first bevel gear, the top end of the stirring tank is screwed with a supporting sleeve, the inside of the supporting sleeve is inserted with the driven shaft, one end of the driven shaft is connected with the blocking column, and the end of the blocking column is attached with a matching pad.
[0014] Further, the surface of the blocking column is provided with grooves, the number of the grooves on each blocking column is two, the side edge of the blocking column and the surface of the matching pad are attached with the inner wall of the quantitative channel, and the other end of the driven shaft is provided with a second bevel gear.
[0015] Further, the first bevel gear and the second bevel gear are engaged, the inside top end of the stirring tank is installed with a conveying pipeline, the top end of the conveying pipeline is installed with a blower, the top end of the blower is aligned with the end of the bottom butt joint sleeve, and the side edge of the first bevel gear is engaged with the two second bevel gears at the same time.
[0016] The beneficial effects of the present application are: 1. The micron-level photovoltaic glass powder mixing and uniform stirring device is provided with a grading tank at the top, a centrifugal component is directly driven to rotate by a power assembly, and the air flow grading process of the feeding raw materials can be realized by cooperating with the blower at the bottom, and in the rotating process, the large-size particles and small-size particles after grading are automatically transported towards the bottom, so that the continuous and uninterrupted feeding and discharging and uniform stirring process are realized, and the preparation process is simplified.
[0017] 2. The micron-level photovoltaic glass powder mixing and uniform stirring device directly transports the feeding raw materials to the middle area of the centrifugal component, and is subjected to the bidirectional influence of centrifugation and air flow extraction at the middle position, so that the separation purpose can be achieved immediately after feeding into the inside, the grading efficiency is improved, and the automatic quantitative feeding and uniform mixing effect of the large-particle powder can also be automatically realized by cooperating with the transmission mechanism at the bottom.
[0018] 3. The micron-level photovoltaic glass powder mixing and uniform stirring device can directly realize the effects of centrifugal grading and quantitative feeding by the single power assembly at the top, the mixing and uniform processing efficiency is improved, the degree of automation is high, and the equipment cost and occupied space are reduced. BRIEF DESCRIPTION OF DRAWINGS
[0019] Figure 1 It is an external structure schematic view of the micron-level photovoltaic glass powder mixing and uniform stirring device. Figure 2 It is a side sectional view of a uniform mixing stirring device for micron-level photovoltaic glass powder of the present application. Figure 3 It is a structural schematic diagram of the power assembly part of the present application. Figure 4 It is a sectional view of the inside of the grading tank of the present application. Figure 2 It is an enlarged view of area A. Figure 5 It is a structural schematic diagram of the transmission mechanism part of the present application. Figure 6 It is an enlarged view of area B. Figure 2 It is an enlarged view of area B. Figure 7 It is a sectional view of the inside of the grading tank of the present application. In the figure: 1, stirring tank; 2, extension plate; 3, stand column; 4, support plate; 5, power assembly; 6, grading tank; 7, injection channel; 8, stirring shaft; 9, stirring rod; 10, centrifugal assembly; 11, centrifugal bin; 12, top layer butt joint sleeve; 13, diffusion pipeline; 14, transmission mechanism; 15, quantitative channel; 16, diffusion port; 17, motor; 18, drive shaft; 19, driving gear; 20, driven gear; 21, movable butt joint hole; 22, ball bearing; 23, supporting plate; 24, fitting plate; 25, fixed butt joint hole; 26, grading bin; 27, driven shaft; 28, support sleeve; 29, second bevel gear; 30, fitting pad; 31, plugging column; 32, groove; 33, guide sleeve; 34, bottom layer butt joint sleeve; 35, air blower; 36, first bevel gear; 37, conveying pipeline. DETAILED DESCRIPTION
[0020] In order to make the technical means, creative features, purposes and effects realized by the present application easy to understand, the present application is further described below in combination with specific embodiments.
[0021] Please refer to Figures 1 to 7The application provides the following technical scheme: a kind of micron photovoltaic glass powder mixing uniform stirring device, including stirring device ontology, the stirring device ontology includes stirring tank 1, grading tank 6, centrifugal component 10 and power component 5, the inside of stirring tank 1 is interspersed with stirring shaft 8, the side of stirring shaft 8 is equipped with stirring rod 9, and the top end of stirring shaft 8 is equipped with bearing, the top end of stirring tank 1 is welded with quantitative channel 15, the top end of quantitative channel 15 is welded with grading tank 6, the inside of grading tank 6 is equipped with centrifugal component 10, the side of stirring tank 1 is integrally formed with extension plate 2, the top end of extension plate 2 is welded with stand 3, the top end of stand 3 is welded with support plate 4, the end of support plate 4 is built with power component 5, the bottom of centrifugal component 10 is embedded with ball 22, and centrifugal component 10 is pressed in the inside of grading tank 6 by ball 22, the middle area below centrifugal component 10 is provided with transmission mechanism 14, the end of transmission mechanism 14 is inserted into the inside of quantitative channel 15, and transmission mechanism 14 and quantitative channel 15 are symmetrically installed on the bottom of grading tank 6 two sides.The mixing uniform stirring device is used for air flow screening grading and quantitative delivery to the glass powder, and finally stirring is carried out to make it homogenization treatment.
[0022] When the application is used, first, superfine material enters high-speed pulverizer for crushing and preliminary mixing;The material after crushing enters air flow grading system through the injection channel 7 at the top, i.e. directly delivered to the centrifugal component 10 at the top, and separated into two different particle size grades of powder by power component 5;Each particle size grade of powder enters the inside of quantitative channel 15, and quantitative channel 15 passes through transmission mechanism 14, according to the preset ratio requirement, control the size of groove 32 on plugging column 31 and the transmission ratio of transmission mechanism 14, and then realize accurate proportioning of each powder;The proportioned powder enters the bottom stirring tank 1 and is fully mixed and uniform, and finally the product meeting the requirements is obtained.
[0023] The centrifugal assembly 10 comprises a centrifugal bin 11, a top butt joint sleeve 12 and a bottom butt joint sleeve 34, the top butt joint sleeve 12 is integrally formed at the top end of the centrifugal bin 11, the bottom of the centrifugal bin 11 is integrally formed with the bottom butt joint sleeve 34, and the two ends of the centrifugal bin 11 are provided with movable butt joint holes 21. The power assembly 5 comprises a motor 17, a driving shaft 18, a driving gear 19 and a driven gear 20, the motor 17 is screwed on the surface of the support plate 4, the output end of the motor 17 is connected with the driving shaft 18, and the tail end of the driving shaft 18 is key-connected with the driving gear 19. The surface of the top butt joint sleeve 12 is welded with the driven gear 20, the driving gear 19 and the driven gear 20 are engaged, the top butt joint sleeve 12 is inserted with the injection channel 7 above, the injection channel 7 is used for conveying the crushed raw materials of photovoltaic glass powder to the inside of the centrifugal assembly 10, the inner wall top end of the centrifugal bin 11 is provided with a diffusion pipeline 13, and the middle of the diffusion pipeline 13 is connected with the inside of the top butt joint sleeve 12. The raw materials are directly conveyed to the middle area of the centrifugal assembly 10 and subjected to the bidirectional influence of centrifugal force and air flow extraction at the middle position, so that the separation purpose can be achieved immediately after being put into the inside, the efficiency of classification is improved, and the automatic quantitative feeding and uniform mixing effect of large particle powder can also be automatically realized by cooperating with the transmission mechanism 14 at the bottom.
[0024] Specifically, after the motor 17 at the top is started, the driving shaft 18 is driven to rotate by the motor 17, the driving shaft 18 drives the driving gear 19 and the driven gear 20 at the tail end to rotate, the driven gear 20 drives the top butt joint sleeve 12 to rotate, that is, the whole centrifugal bin 11 is controlled to rotate, so that the crushed materials put into the inside can diffuse towards the two ends under the centrifugal force, and the air blower 35 at the bottom is started to blow the air flow from the inside towards the bottom. In this process, the centrifugal force on the large / heavy particles is much larger than the air flow suction force. They are mainly disturbed by the centrifugal force and are thrown to the periphery of the centrifugal bin 11 and fall or slide along the inner wall at the tail end. Finally, they pass through the centrifugal bin 11 from the outside into the inside of the classification tank 6; small / light particles: the air flow suction force on them is greater than the centrifugal force. They are mainly affected by the suction force and are sucked into the bottom butt joint sleeve 34 and finally conveyed towards the stirring tank 1 at the bottom through the transmission mechanism 14.
[0025] The grading tank 6 comprises a supporting plate 23, a fitting plate 24 and grading bins 26. The fitting plate 24 is arranged on the inner side of the grading tank 6, and the two ends of the fitting plate 24 are provided with grading bins 26. The inner wall of each grading bin 26 is provided with a fixed butt joint hole 25. The bottom of the grading tank 6 is integrally formed with the supporting plate 23. The centrifugal assembly 10 is pressed on the supporting plate 23 through the bottom ball 22, and the end of the centrifugal bin 11 is used to press on the surface of the fitting plate 24. The top and middle region of the bottom of the grading tank 6 are in an open state. The grading tank 6 is fixed as a whole with the lower stirring tank 1 through the quantitative channel 15. The grading bins 26 are arranged on both sides of the grading tank 6 in a symmetrical manner. The gap is arranged between the top of the two ends of the centrifugal bin 11 and the inner wall top end of the grading tank 6. The grading tank 6 is arranged on the top. The centrifugal assembly 10 is directly driven to rotate by the power assembly 5. The air flow grading process of the feeding raw material can be realized by cooperating with the bottom air blower 35. During the rotation process, the large and small size particles after grading are automatically transported towards the bottom, so as to realize the continuous and uninterrupted feeding and discharging and uniform stirring process, and the material preparation process is simplified.
[0026] Specifically, during the high-speed rotation of the centrifugal bin 11, the movable butt joint hole 21 at the end of the bottom is rotated along the surface of the fitting plate 24 until the movable butt joint hole 21 is aligned with the fixed butt joint hole 25, so that the large particle powder in the centrifugal bin 11 enters the inside of the grading bin 26 through the two holes in sequence, and finally enters the inside of the quantitative channel 15 from the bottom of the grading bin 26 for subsequent quantitative process. The intermediate small particle powder is affected by the air flow at the moment when it is sprayed from the diffusion pipe 13 towards the bottom, so that it can be directly sucked towards the middle region, so as to achieve the grading purpose.
[0027] The transmission mechanism 14 comprises a driven shaft 27, a blocking column 31, a first bevel gear 36 and a second bevel gear 29, the surface of the bottom butt joint sleeve 34 is keyed with the first bevel gear 36, the top end of the stirring tank 1 is screwed with a supporting sleeve 28, the inside of the supporting sleeve 28 is inserted with the driven shaft 27, one end of the driven shaft 27 is connected with the blocking column 31, the end of the blocking column 31 is attached with a matching pad 30. The surface of the blocking column 31 is provided with a groove 32, and the number of the groove 32 on each blocking column 31 is two, the side of the blocking column 31 and the surface of the matching pad 30 are matched with the inner wall of the quantitative channel 15, the other end of the driven shaft 27 is provided with the second bevel gear 29. The first bevel gear 36 and the second bevel gear 29 are engaged, the inside top end of the stirring tank 1 is installed with a conveying pipeline 37, the top end of the conveying pipeline 37 is installed with a blower 35, the top end of the blower 35 is aligned with the end of the bottom butt joint sleeve 34, and the side of the first bevel gear 36 is engaged with the two second bevel gears 29 at the same time. Through the single power assembly 5 at the top, the effects of centrifugal classification and quantitative conveying can be directly realized, the efficiency of mixing processing is improved, the degree of automation is high, and the equipment cost and occupied space are reduced.
[0028] Specifically, when the power assembly 5 at the top is started to drive the whole centrifugal assembly 10 to operate, the first bevel gear 36 is also driven to rotate through the bottom butt joint sleeve 34, the two second bevel gears 29 on the sides are driven to rotate by the first bevel gear 36, and the end blocking column 31 is driven to rotate through the rotation of the driven shaft 27. Since the blocking column 31 is inserted into the inside of the quantitative channel 15 through the guide sleeve 33, when one of the grooves 32 on the surface is rotated vertically upward during the rotation of the blocking column 31, the larger particle powder can fall into the inside of the groove 32. With the continuous rotation of the driven shaft 27, the groove 32 is rotated vertically downward, at this time, the powder in the groove 32 after quantitative can be put into the inside of the stirring tank 1 at the bottom, and the purpose of quantitative conveying is achieved. The bottom butt joint sleeve 34 is also directly aligned with the blower 35 at the bottom, so that the small particles in the centrifugal bin 11 can be directly extracted through the blower 35 and conveyed into the conveying pipeline 37 below, and then diffused into the inside of the stirring tank 1 through the diffusion port 16 at the bottom end of the conveying pipeline 37. The top end of the stirring shaft 8 is supported below the diffusion port 16 through the bearing, for providing stable support.
[0029] The above shows and describes the basic principles and main features of the present application and the advantages of the present application. It is obvious for those skilled in the art that the present application is not limited to the details of the above exemplary embodiments, and the present application can be realized in other specific forms without departing from the spirit or essential characteristics of the present application.
[0030] Furthermore, it should be understood that although the specification is described in terms of embodiments, not every embodiment includes every feature described. The specification can include implicit combinations of explicitly mentioned features and / or explicit combinations of implicitely mentioned features. Each embodiment depends on the explicit combinations of features and / or the implicit combinations of features made specifically within that embodiment, and each such embodiment can be combined with every other such embodiment to create further embodiments.
Claims
1. A device for uniformly mixing micron-sized photovoltaic glass powder, comprising a stirring device body, characterized in that: The stirring device body comprises a stirring tank (1), a grading tank (6), a centrifugal assembly (10) and a power assembly (5); a stirring shaft (8) is inserted into the interior of the stirring tank (1); a stirring rod (9) is installed on the side of the stirring shaft (8); and a bearing is sleeved on the top end of the stirring shaft (8); a quantitative channel (15) is welded to the top end of the quantitative channel (15); a grading tank (6) is welded to the top end of the quantitative channel (15); a centrifugal assembly (10) is installed on the inner side of the grading tank (6); an extension plate (2) is integrally formed on the side of the stirring tank (1); and the top of the extension plate (2) is provided with a cylindrical roller. A column (3) is welded to the end of the column (3), a support plate (4) is welded to the top of the column (3), a power assembly (5) is built on the end of the support plate (4), a ball (22) is embedded in the bottom of the centrifugal assembly (10), and the centrifugal assembly (10) is pressed against the inner side of the classification tank (6) by the ball (22), a transmission mechanism (14) is provided in the middle area below the centrifugal assembly (10), the end of the transmission mechanism (14) is inserted into the interior of the quantitative channel (15), and the transmission mechanism (14) and the quantitative channel (15) are both symmetrically installed on both sides of the bottom of the classification tank (6).
2. The device for uniformly mixing and stirring micron-sized photovoltaic glass powder according to claim 1, characterized in that: The centrifugal assembly (10) comprises a centrifugal chamber (11), a top docking sleeve (12) and a bottom docking sleeve (34); the top docking sleeve (12) is integrally formed on the top of the centrifugal chamber (11); the bottom of the centrifugal chamber (11) is integrally formed with the bottom of the centrifugal chamber (34); and movable docking holes (21) are provided at the bottoms of both ends of the centrifugal chamber (11).
3. The device for uniformly mixing and stirring micron-sized photovoltaic glass powder according to claim 2, characterized in that: The power assembly (5) comprises a motor (17), a drive shaft (18), a driving gear (19) and a driven gear (20); the motor (17) is screwed to the surface of the support plate (4); the output end of the motor (17) is connected to the drive shaft (18); and the end key of the drive shaft (18) is connected to the driving gear (19).
4. The device for uniformly mixing and stirring micron-sized photovoltaic glass powder according to claim 3, characterized in that: A driven gear (20) is welded to the surface of the top-layer docking sleeve (12), and the driving gear (19) and the driven gear (20) are meshed with each other. An injection channel (7) is inserted above the top-layer docking sleeve (12), and the injection channel (7) is used to transport the raw materials after the photovoltaic glass powder is crushed into the interior of the centrifugal assembly (10). A diffusion pipe (13) is installed at the top end of the inner wall of the centrifugal chamber (11), and the middle of the diffusion pipe (13) is connected to the interior of the top-layer docking sleeve (12).
5. The device for uniformly mixing and stirring micron-sized photovoltaic glass powder according to claim 3, characterized in that: The grading tank (6) comprises a supporting plate (23), a laminating plate (24) and a grading bin (26); the laminating plate (24) is arranged on the inner side of the grading tank (6); grading bins (26) are arranged at both ends of the laminating plate (24); and a fixing docking hole (25) is opened on the inner wall of each grading bin (26).
6. The device for uniformly mixing and stirring micron-sized photovoltaic glass powder according to claim 5, characterized in that: The bottom of the grading tank (6) is integrally formed with a support plate (23), the centrifugal assembly (10) is pressed onto the support plate (23) via the ball bearings (22) at the bottom, and the end of the centrifugal chamber (11) is used to press onto the surface of the laminating plate (24), and the top and bottom middle areas of the grading tank (6) are both in an open state.
7. The device for uniformly mixing and stirring micron-sized photovoltaic glass powder according to claim 6, characterized in that: The grading tank (6) is fixed as a whole with the stirring tank (1) below via a quantitative channel (15); the grading bin (26) is symmetrically arranged on both sides of the grading tank (6); and gaps are provided between the top ends of the centrifugal bin (11) and the top end of the inner wall of the grading tank (6).
8. The device for uniformly mixing and stirring micron-sized photovoltaic glass powder according to claim 5, characterized in that: The transmission mechanism (14) includes a driven shaft (27), a blocking column (31), a first bevel gear (36) and a second bevel gear (29); the surface key of the bottom docking sleeve (34) is connected to the first bevel gear (36); the top end of the mixing tank (1) is screwed with a support sleeve (28); the interior of the support sleeve (28) is penetrated by the driven shaft (27); one end of the driven shaft (27) is connected to the blocking column (31); the end of the blocking column (31) is attached with a fitting pad (30).
9. The device for uniformly mixing and stirring micron-sized photovoltaic glass powder according to claim 8, characterized in that: The surface of the blocking column (31) is provided with a groove (32), and the number of grooves (32) on each blocking column (31) is two. The side of the blocking column (31) and the surface of the fitting pad (30) are both fitted with the inner wall of the quantitative channel (15). The other end of the driven shaft (27) is provided with a second bevel gear (29).
10. The device for uniformly mixing and stirring micron-sized photovoltaic glass powder according to claim 9, characterized in that: The first bevel gear (36) is meshed with the second bevel gear (29). A delivery pipe (37) is installed at the top of the inner side of the mixing tank (1). A blower (35) is installed at the top of the delivery pipe (37). The top of the blower (35) is aligned with the end of the bottom docking sleeve (34). The side of the first bevel gear (36) is meshed with the two second bevel gears (29) at the same time.
Citation Information
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