Vapor phase method white carbon black powder bin
Patent Information
- Application Number
- CN202411793215.3
- Authority / Receiving Office
- CN · China
- Patent Type
- Applications(China)
- Current Assignee / Owner
- Filing Date
- 2024-12-09
- Publication Date
- 2025-01-07
- Estimated Expiration
- Not applicable · inactive patent
AI Technical Summary
The gas-phase method white carbon black powder easily forms arches due to small particles and density, resulting in uneven discharge. The existing arch breaking method will lead to loose powder, decrease in stacking density and contamination of acidic substances, increasing the exhaust gas treatment pressure.
A gas-phase white carbon black powder silo including a support frame, storage tank and a broken arch discharge stirring system is designed. The drive assembly, discharge assembly, broken arch assembly and agitation assembly are used to drive stirring through the drive gear and rotating parts. The parts are rotated and rotated, breaking the plate powder and achieving uniform discharge through the discharge spiral.
The gas-phase white carbon black that effectively breaks the arch and breaks the agglomerates ensures uniformity of discharge, reduces the exhaust gas treatment pressure, and improves the effective capacity of the silo and the quality of subsequent vacuum packaging.
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Figure CN119262579A_ABST
Abstract
Description
Technical Field
[0001] The invention relates to the technical field of material storage, and in particular to a fumed silica powder silo. Background Art
[0002] Fumed silica is fumed silica, chemically known as hydrated silicon dioxide, with a chemical formula of SiO 2 ·nH 2 O is an extremely fine nano-scale amorphous silicon dioxide obtained by high-temperature hydrolysis of halosilanes in a hydrogen-oxygen flame. It has a small particle size, uniform particle size distribution, and a large specific surface area, so it has a high surface activity. Fumed silica is widely used in polymer composite materials, silicone rubber, coatings, electronic packaging materials, colloidal batteries, ceramics, plastics, fiberglass, sealants, papermaking, food, cosmetics, gel coat resins, chemical mechanical polishing and other industries, and can play a role in reinforcement, thickening, thixotropy, and matting.
[0003] After the production of fumed silica is completed, it needs to be stored in the silo and then evenly transported to the vacuum packaging machine; during the transportation process, it is necessary to ensure that the material is discharged evenly, otherwise it is easy to cause problems such as empty vacuum packaging bags and insufficient loading. Due to the small particle size and light density of fumed silica powder (bulk density 200-400kg / m³), it is very easy to form arches and bridges during the discharging process, resulting in uneven discharging or even failure to discharge. In addition, because there will be acidic substances remaining in the production process of silica, the storage tanks are mostly made of fiberglass, and it is impossible to use vibration and other methods to break the arch; the existing arch breaking method is the air-blowing arch breaking method. Although the air-blast arch-breaking method can effectively break the arches and discharge the material, it also has the following problems: 1) When using the air-blast arch-breaking method, the fumed silica powder is likely to become loose, causing the bulk density to drop again, reducing the effective capacity of the silo, and is not good for the later vacuum packaging; 2) During the production process of fumed silica, some acidic substances will remain. When the gas is discharged by the air-blast arch-breaking method, the fumed silica powder and some acidic substances will be mixed in, which need to be treated before being discharged, increasing the tail gas treatment pressure. In addition, due to the interaction between particles, the influence of temperature and humidity, fumed silica is prone to agglomeration, which will also lead to uneven discharge or even failure to discharge. Summary of the invention
[0004] In view of this, the object of the present invention is to provide a fumed silica powder silo that can solve or at least alleviate the above-mentioned problems, so as to effectively break up the arches and disperse the agglomerated fumed silica, ensure the uniform discharge of the fumed silica, and reduce the exhaust gas treatment pressure.
[0005] The technical solution provided by the present invention is: a fumed silica powder silo, comprising a support frame, a storage tank mounted on the support frame, and an arch-breaking discharging and stirring system installed in the storage tank; the arch-breaking discharging and stirring system comprises a driving component, a discharging component, an arch-breaking component and a stirring component; the driving component can drive the discharging component to rotate relative to the storage tank; the discharging component is rotatably mounted on the discharging port of the discharging hopper of the storage tank; the arch-breaking component comprises a rotating shaft connected to the discharging component, a plurality of first arch-breaking components mounted on the rotating shaft, and a first arch-breaking component mounted on the rotating shaft and a second arch-breaking member located below the first arch-breaking member, and an intermediate support member installed on the inner side of the tank body of the storage tank; the stirring assembly includes a driving gear, a rotating member, a driven gear and a stirring member; the driving gear is sleeved on the rotating shaft and is located above the intermediate support member; the rotating member is installed on the rotating shaft; the driven gear is engaged with the driving gear; the stirring member is installed on the driven gear; when the rotating shaft drives the driving gear and the rotating member to rotate, under the action of the driving gear and the rotating member, the stirring member can revolve relative to the rotating shaft and rotate at the same time.
[0006] In some embodiments, a groove is provided on the inner side of the tank body, and the groove is formed by being recessed radially from the inner side of the tank body along the tank body; the stirring assembly also includes a support assembly, which is installed on the end of the stirring member away from the driven gear, and the support assembly can partially engage with the groove.
[0007] In some embodiments, the rotating member includes a rotating member body and a bottom plate; the rotating member body is a cylindrical body with one end open; the bottom plate cover is arranged on the open end of the rotating member body, and a through hole is opened in the center of the bottom plate for the rotating shaft to pass through; the rotating member body is provided with a top plate, a mounting portion and an arc-shaped portion; the top plate is the closed end of the rotating member body, the outer side of the top plate is conical, and a blind hole is provided on the inner side of the top plate, and the rotating member is installed on the rotating shaft through the blind hole; the mounting portion extends vertically downward from the lower side of the top plate, and the mounting portion is flat; the arc-shaped portion is provided between two adjacent mounting portions, and a plurality of stirring protrusions are provided on the outer side of the arc-shaped portion; a mounting hole is opened in the center of the mounting portion, and the stirring member can be rotatably mounted on the mounting hole.
[0008] In some embodiments, the stirring member includes a stirring support shaft rotatably mounted on the mounting hole, and crushing teeth arranged on the outer peripheral side of the stirring support shaft; the stirring support shaft extends into the rotating member through the mounting hole, and the driven gear is installed on the axial end of the stirring support shaft located in the rotating member; a coupling groove is provided on the other axial end of the stirring support shaft away from the rotating member, and the coupling groove is formed by a radial recess along the stirring support shaft, and the support assembly is engaged on the coupling groove.
[0009] In some embodiments, the support assembly includes a support member and a rotating wheel; the support member is a hollow cylinder with one end open, and a protrusion is provided on the inner side of the open end of the support member, and the protrusion is engaged in the engaging groove; a connecting column is installed on the outer side of the closed end of the support member, and the connecting column is arranged along the axial direction of the tank body, and a rotating wheel is rotatably mounted on the connecting column, and the rotating wheel is partially engaged in the groove of the tank body.
[0010] In some embodiments, the discharging assembly includes a discharging pipe rotatably supported on the discharging port of the discharging hopper, a discharging support member arranged on the inner side of the discharging pipe, a transmission shaft installed on the discharging support member, and a discharging spiral arranged on the outer side of the transmission shaft; the transmission shaft extends upward through the discharging port and is connected to the arch breaking assembly.
[0011] In some embodiments, one end of the rotating shaft adjacent to the transmission shaft is connected to the transmission shaft via a coupling, and the other end of the rotating shaft away from the transmission shaft is rotatably mounted on the intermediate support member via a bearing.
[0012] In some embodiments, the intermediate support member includes a ring body mounted on the inner side of the tank body, and a plurality of support ribs disposed on the inner side of the ring body.
[0013] In some embodiments, the plurality of first arch-breaking members are staggeredly distributed along the axial direction of the rotating shaft; each of the plurality of first arch-breaking members includes a screw mounted on the rotating shaft, and a single-sided blade mounted on one end of the screw away from the rotating shaft.
[0014] In some embodiments, the second arch-breaking member is C-shaped; two second arch-breaking members are disposed on the rotating shaft, and the two second arch-breaking members are disposed opposite to each other along the radial direction of the rotating shaft.
[0015] Compared with the prior art, the present invention has at least the following beneficial effects: 1. The fumed silica powder silo provided by the present invention can effectively break up the arches and disperse the agglomerated fumed silica, ensure the uniform discharge of the fumed silica, and reduce the tail gas treatment pressure.
[0016] 2. In the present invention, when the rotating shaft drives the driving gear and the rotating member to rotate, under the action of the driving gear and the rotating member, the stirring member can revolve relative to the rotating shaft and rotate at the same time, so as to break up the compacted powder in the storage tank, so as to preliminarily ensure the uniform discharge of the fumed silica.
[0017] 3. The support assembly in the present invention can support the other axial end of the stirring support shaft away from the rotating member to prevent the stirring support shaft from deforming, and can not hinder the self-rotation of the stirring member, thereby increasing the service life of the stirring member.
[0018] 4. In the present invention, the fumed silica in the storage tank passes through the stirring component, the arch breaking component and the discharging component in sequence. The stirring component can break up the compacted powder. The arch breaking component can break the arches of the powder stirred by the stirring component and further stir the powder to achieve the effect of breaking the arches and promoting the discharge of the fumed silica. The discharging component can evenly discharge the powder after the arch breaking and stirring by the arch breaking component. BRIEF DESCRIPTION OF THE DRAWINGS
[0019] Figure 1 A three-dimensional diagram of a fumed silica powder silo according to an embodiment of the present invention is shown.
[0020] Figure 2 Shows Figure 1 An exploded view of a fumed silica powder silo is shown with some components omitted.
[0021] Figure 3 Shows Figure 1 A plan view of a fumed silica powder silo is shown.
[0022] Figure 4 Shown along Figure 3 A cross-sectional view along line AA in which some components are omitted.
[0023] Figure 5 Shows Figure 1 The three-dimensional diagram of the arch-breaking discharging and stirring system of the fumed silica powder silo is shown, in which some components are omitted.
[0024] Figure 6 Shows Figure 5 A plan view of the arch-breaking discharging and mixing system is shown.
[0025] Figure 7 Shows Figure 5 The exploded view of the arch-breaking discharging and mixing system is shown.
[0026] Figure 8 Shows Figure 5 The exploded view of the stirring assembly of the arch-breaking discharging stirring system is shown, in which some parts are further omitted.
[0027] Fig. 9 An exploded view of the rotating parts of the stirring assembly is shown.
[0028] Explanation of reference numerals: 1-storage tank; 11-storage tank body; 12-groove; 13-discharging hopper; 2-arch breaking discharging stirring system; 21-driving assembly; 22-discharging assembly; 221-discharging pipe; 222-discharging support; 223-transmission shaft; 224-discharging spiral; 23-arch breaking assembly; 231-rotating shaft; 232-first arch breaking member; 233-second arch breaking member; 234-middle support member; 341-ring body; 342-support rib; 235-bearing ;24-stirring assembly;41-driving gear;42-rotating member;421-rotating member body;422-top plate;423-mounting portion;424-mounting hole;425-arc-shaped portion;426-stirring protrusion;427-bottom plate;428-blind hole;43-driven gear;44-stirring member;441-stirring support shaft;442-crushing tooth;443-engaging groove;45-support assembly;51-support member;52-rotating wheel;53-connecting column;3-support frame. DETAILED DESCRIPTION
[0029] The present invention is further described below in conjunction with the accompanying drawings and specific embodiments.
[0030] It should be noted that the following detailed descriptions are all illustrative and intended to provide further explanation of the present invention. Unless otherwise specified, all technical and scientific terms used herein have the same meanings as those commonly understood by those skilled in the art to which the present invention belongs.
[0031] It should be noted that the terms used herein are only for describing specific embodiments and are not intended to limit exemplary embodiments according to the present invention. As used herein, unless the context clearly indicates otherwise, the singular form is also intended to include the plural form. In addition, it should be understood that when the terms "comprising" and / or "including" are used in this specification, it indicates the presence of features, steps, operations, devices, components and / or combinations thereof.
[0032] In the present invention, terms such as "upper", "lower", "left", "right", "front", "back", "vertical", "horizontal", "side", "bottom", etc. indicate directions or positional relationships based on the directions or positional relationships shown in the accompanying drawings. They are relational words determined only for the convenience of describing the structural relationships of the various parts or elements of the present invention, and do not specifically refer to any part or element in the present invention and should not be understood as limitations on the present invention.
[0033] In the present invention, terms such as "fixed connection", "connected", "connection", etc. should be understood in a broad sense, indicating that it can be fixedly connected, integrally connected or detachably connected; it can be directly connected or indirectly connected through an intermediate medium. Relevant scientific research or technical personnel in this field can determine the specific meanings of the above terms in the present invention according to specific circumstances, and they should not be understood as limiting the present invention.
[0034] Also refer to Figures 1 to 4 The fumed silica powder silo provided by the present invention includes a support frame 3, a storage tank 1 installed on the support frame 3, and a broken arch discharging stirring system 2 installed in the storage tank 1. The support frame 3 can adopt an existing structure in the prior art, which is not described in detail here. The storage tank 1 includes a storage tank body 11, a discharge hopper 13 arranged on the storage tank body 11, and a groove 12 arranged on the inner side of the storage tank body 11. The storage tank body 11 is roughly a hollow cylinder with one end open. The discharge hopper 13 is roughly funnel-shaped and is arranged on the open end of the storage tank body 11. The groove 12 is arranged on the inner side of the storage tank body 11 at one end adjacent to the discharge hopper 13. The groove 12 is formed by being recessed from the inner side of the storage tank body 11 along the radial direction of the storage tank body 11.
[0035] The arch-breaking discharging and stirring system 2 includes a driving component 21, a discharging component 22, an arch-breaking component 23 and a stirring component 24. The driving component 21 is mounted on the support frame 3 and is located below the storage tank 1. The driving component 21 can drive the discharging component 22 to rotate relative to the storage tank 1. The driving component 21 can adopt the existing structure in the prior art. Preferably, the driving component 21 includes a motor, a gear reducer, a belt reducer and a slewing support. The driving component 21 uses the motor as a power source, and adjusts the speed and torque of the motor to the values required for the operation of the arch-breaking discharging and stirring system 2 through the gear reducer, the belt reducer and the slewing support. The motor, the gear reducer, the belt reducer and the slewing support can all adopt the existing structure in the prior art, which will not be described in detail here.
[0036] Also refer to Figures 4 to 7, the discharge assembly 22 is rotatably mounted on the discharge port of the discharge hopper 13. The discharge assembly 22 includes a discharge pipe 221 rotatably supported on the discharge port of the discharge hopper 13, a discharge support 222 arranged on the inner side of the discharge pipe 221, a transmission shaft 223 installed on the discharge support 222, and a discharge spiral 224 arranged on the outer side of the transmission shaft 223. Preferably, the discharge pipe 221 is roughly a hollow pipe with two ends open. More preferably, the discharge pipe 221 is a titanium tube. The discharge pipe 221 is connected to the slewing support of the drive assembly 21. During the operation of the arch-breaking discharge mixing system 2, the discharge pipe 221 is driven to rotate by the slewing support, and the lower end of the discharge pipe 221 is connected to the rotary joint and docked to the subsequent pipeline system. The upper end of the discharge pipe 221 passes through the discharge port of the discharge hopper 13 of the storage tank 1, and the discharge pipe 221 and the discharge port are sealed by a packing seal. The discharge pipe 221 is used to transport materials and can also drive the arch-breaking assembly 23 to rotate relative to the discharge hopper 13. The discharge support 222 is between the inner side of the discharge pipe 221 and the drive shaft 223. Preferably, the discharge support 222 is roughly fan-shaped. The three discharge supports 222 are evenly spaced around the circumference of the discharge pipe 221. When the discharge pipe 221 drives the drive shaft 223 to rotate relative to the discharge hopper 13 through the discharge support 222, the discharge screw 224 on the drive shaft 223 also rotates relative to the discharge hopper 13, so that the fumed silica in the storage tank 1 can be discharged through the gap between the discharge supports 222. The drive shaft 223 extends upward through the discharge port and is connected to the arch-breaking assembly 23.
[0037] The arch breaking assembly 23 includes a rotating shaft 231 connected to the transmission shaft 223, a plurality of first arch breaking members 232 mounted on the rotating shaft 231, a second arch breaking member 233 mounted on the rotating shaft 231 and located below the first arch breaking member 232, and an intermediate support member 234 mounted on the inner side of the storage tank body 11. Preferably, one end of the rotating shaft 231 adjacent to the transmission shaft 223 is connected to the transmission shaft 223 through a coupling, and the other end of the rotating shaft 231 away from the transmission shaft 223 is rotatably mounted on the intermediate support member 234 through a bearing 235. The plurality of first arch breaking members 232 are staggered along the axial direction of the rotating shaft 231. Each of the plurality of first arch breaking members 232 includes a screw mounted on the rotating shaft 231, and a single-sided paddle mounted on one end of the screw away from the rotating shaft 231. The plurality of first arch breaking members 232 can stir the fumed silica in the storage tank 1 to achieve the function of arch breaking and promoting the discharge of fumed silica. The second arch-breaking member 233 is roughly C-shaped. Preferably, two second arch-breaking members 233 are arranged on the rotating shaft 231, and the two second arch-breaking members 233 are arranged opposite to each other along the radial direction of the rotating shaft 231. The intermediate support member 234 includes a ring body 341 mounted on the inner side of the storage tank body 11, and a plurality of support ribs 342 arranged on the inner side of the ring body 341. Preferably, the number of the plurality of support ribs 342 is 3. The upper side of each of the plurality of support ribs 342 is arranged in a triangular shape to prevent obstruction of the downward movement of the powder. A mounting hole is provided at the intersection of the plurality of support ribs 342, and the bearing 235 is installed in the mounting hole. The rotating shaft 231 protrudes upward from the intermediate support member 234. The stirring assembly 24 is rotatably mounted above the intermediate support member 234 through the rotating shaft 231.
[0038] The stirring assembly 24 includes a driving gear 41, a rotating member 42, a driven gear 43, a stirring member 44 and a supporting assembly 45. The driving gear 41 is sleeved on the rotating shaft 231 and is located above the intermediate supporting member 234, and can rotate with the rotation of the rotating shaft 231. The rotating member 42 is mounted on the rotating shaft 231. The driven gear 43 is engaged with the driving gear 41. Preferably, the driving gear 41 and the driven gear 43 are both bevel gears. The stirring member 44 is mounted on the driven gear 43. Preferably, the number of the stirring members 44 is three. The supporting assembly 45 is mounted on one end of the stirring member 44 away from the driven gear 43, and the supporting assembly 45 can partially engage with the groove 12 of the storage tank body 11. When the rotating shaft 231 drives the driving gear 41 and the rotating member 42 to rotate, under the action of the driving gear 41 and the rotating member 42, the stirring member 44 can revolve relative to the rotating shaft 231 and rotate at the same time, so as to break up the compacted powder in the storage tank 1, so as to preliminarily ensure the uniform discharge of the fumed silica.
[0039] Also refer to Fig. 9The rotating member 42 includes a rotating member body 421 and a bottom plate 427. The rotating member body 421 is roughly cylindrical with one end open. The bottom plate 427 is covered on the open end of the rotating member body 421, and a through hole is opened in the center of the bottom plate 427 for the rotating shaft 231 to pass through. The rotating member 42 can prevent the driving gear 41 and the driven gear 43 from being affected by the powder. The rotating member body 421 is provided with a top plate 422, a mounting portion 423 and an arc portion 425. The top plate 422 is the closed end of the rotating member body 421. The outer side of the top plate 422 is roughly conical to avoid the accumulation of powder. The inner side of the top plate 422 is provided with a blind hole 428, through which the rotating member 42 is mounted on the rotating shaft 231. The mounting portion 423 extends vertically downward from the lower side of the top plate 422. The mounting portion 423 is roughly flat. Preferably, the number of mounting portions 423 is three. The arc portion 425 is disposed between two adjacent mounting portions 423. A plurality of stirring protrusions 426 are disposed on the outer side of the arc portion 425. A mounting hole 424 is provided at the center of the mounting portion 423, and the stirring member 44 is rotatably mounted on the corresponding mounting hole 424.
[0040] Also refer to Figure 4 and Figure 8 The stirring member 44 includes a stirring support shaft 441 rotatably mounted on the mounting hole 424, and a crushing tooth 442 provided on the outer peripheral side of the stirring support shaft 441. The stirring support shaft 441 extends through the mounting hole 424 into the rotating member 42, and the driven gear 43 is installed on the axial end of the stirring support shaft 441 located in the rotating member 42. An engagement groove 443 is provided on the other axial end of the stirring support shaft 441 away from the rotating member 42, and the engagement groove 443 is recessed along the radial direction of the stirring support shaft 441. The support assembly 45 is engaged with the engagement groove 443.
[0041] The support assembly 45 includes a support member 51 and a rotating wheel 52. The support member 51 is generally a hollow cylinder with one end open. A protrusion is provided on the inner side of the open end of the support member 51, and the protrusion is engaged in the engaging groove 443. When the stirring member 44 rotates, the stirring support shaft 441 can rotate relative to the support member 51, driving the crushing teeth 442 to break up the compacted powder. In other words, the other axial end of the stirring support shaft 441 away from the rotating member 42 is rotatably engaged in the support member 51. A connecting column 53 is installed on the outer side of the closed end of the support member 51, and the connecting column 53 is arranged along the axial direction of the storage tank body 11. The rotating wheel 52 is rotatably mounted on the connecting column 53, and the rotating wheel 52 is partially engaged in the groove 12 of the storage tank body 11. When the stirring member 44 revolves relative to the rotating shaft 231, the stirring support shaft 441 drives the rotating wheel 52 to move in the groove 12. The support assembly 45 can support the other axial end of the stirring support shaft 441 away from the rotating member 42 to prevent the stirring support shaft 441 from deforming, and can not hinder the self-rotation of the stirring member 44, thereby increasing the service life of the stirring member 44.
[0042] When in use, the fumed silica in the storage tank 1 passes through the stirring component 24, the arch breaking component 23 and the discharging component 22 in sequence, wherein the stirring component 24 can break up the compacted powder, the arch breaking component 23 can break the arch and further stir the powder after stirring by the stirring component 24 to achieve the function of arch breaking and promoting the discharge of fumed silica, and the discharging component 22 can evenly discharge the powder after the arch breaking component 23 is broken and stirred. During this process, the driving component 21 drives the discharging component 22 to operate, and the discharging component 22 drives the arch breaking component 23 and the stirring component 24 to operate at the same time. Specifically, the discharge pipe 221 of the discharge component 22 drives the transmission shaft 223 to rotate relative to the discharge hopper 13 through the discharge support 222, and the transmission shaft 223 drives the rotating shaft 231 to rotate, and at the same time, the first arch-breaking member 232 and the second arch-breaking member 233 on the rotating shaft 231 rotate relative to the discharge hopper 13, and the transmission shaft 223 drives the driving gear 41 and the rotating member 42 of the stirring component 24 to rotate relative to the storage tank body 11. Under the action of the driving gear 41 and the rotating member 42, the stirring member 44 can revolve relative to the rotating shaft 231 and rotate at the same time, so as to be able to break the compacted powder in the storage tank 1, so as to preliminarily ensure the uniform discharge of the fumed silica; the fumed silica that is dispersed and stirred by the stirring member 44 is broken and stirred at the first arch-breaking member 232 and the second arch-breaking member 233 in turn, and the fumed silica that has been broken and stirred is discharged through the discharge spiral 224 through the gap between the discharge support members 222.
[0043] The above description is only a preferred embodiment of the present invention and is not intended to limit the present invention. For those skilled in the art, the present invention may have various modifications and variations. Any modification, equivalent replacement, improvement, etc. made within the spirit and principle of the present invention shall be included in the protection scope of the present invention.
Claims
1. A fumed silica powder silo, comprising a support frame, a storage tank mounted on the support frame, and a broken arch discharging stirring system installed in the storage tank; characterized in that: The arch-breaking discharging and stirring system comprises a driving assembly, a discharging assembly, an arch-breaking assembly and a stirring assembly; the driving assembly can drive the discharging assembly to rotate relative to the storage tank; the discharging assembly is rotatably mounted on the discharge port of the discharging hopper of the storage tank; the arch-breaking assembly comprises a rotating shaft connected to the discharging assembly, a plurality of first arch-breaking members mounted on the rotating shaft, a second arch-breaking member mounted on the rotating shaft and located below the first arch-breaking members, and an intermediate support member mounted on the inner side of the storage tank body of the storage tank; the stirring assembly comprises a driving gear, a rotating member, a driven gear and a stirring member; the driving gear is sleeved on the rotating shaft and located above the intermediate support member; the rotating member is mounted on the rotating shaft; the driven gear is engaged with the driving gear; The stirring member is mounted on the driven gear; when the rotating shaft drives the driving gear and the rotating member to rotate, under the action of the driving gear and the rotating member, the stirring member can revolve relative to the rotating shaft and rotate at the same time.
2. The fumed silica powder silo according to claim 1, characterized in that: A groove is provided on the inner side of the tank body, and the groove is recessed radially from the inner side of the tank body; the stirring assembly also includes a support assembly, which is installed on the end of the stirring member away from the driven gear, and the support assembly can partially engage with the groove.
3. The fumed silica powder silo according to claim 2, characterized in that: The rotating member includes a rotating member body and a bottom plate; the rotating member body is a cylindrical body with an open end; the bottom plate cover is arranged on the open end of the rotating member body, and a through hole is opened in the center of the bottom plate for the rotating shaft to pass through; the rotating member body is provided with a top plate, a mounting portion and an arc-shaped portion; the top plate is the closed end of the rotating member body, the outer side of the top plate is conical, and a blind hole is provided on the inner side of the top plate, and the rotating member is mounted on the rotating shaft through the blind hole; the mounting portion extends vertically downward from the lower side of the top plate, and the mounting portion is in the shape of a flat plate; the arc-shaped portion is provided between two adjacent mounting portions, and a plurality of stirring protrusions are provided on the outer side of the arc-shaped portion; a mounting hole is opened in the center of the mounting portion, and the stirring member can be rotatably mounted on the mounting hole.
4. The fumed silica powder silo according to claim 3, characterized in that: The stirring member includes a stirring support shaft rotatably mounted on the mounting hole, and a crushing tooth arranged on the outer peripheral side of the stirring support shaft; the stirring support shaft extends into the rotating member through the mounting hole, and the driven gear is mounted on the axial end of the stirring support shaft located in the rotating member; a coupling groove is provided on the other axial end of the stirring support shaft away from the rotating member, and the coupling groove is formed by a radial recess along the stirring support shaft, and the support assembly is engaged on the coupling groove.
5. The fumed silica powder silo according to claim 4, characterized in that: The support assembly includes a support member and a rotating wheel; the support member is a hollow cylinder with one end open, and a protrusion is provided on the inner side of the open end of the support member, and the protrusion is engaged in the engaging groove; a connecting column is installed on the outer side of the closed end of the support member, and the connecting column is arranged along the axial direction of the tank body, and a rotating wheel is rotatably mounted on the connecting column, and the rotating wheel is partially engaged in the groove of the tank body.
6. The fumed silica powder silo according to claim 1, characterized in that: The discharging assembly includes a discharging pipe rotatably supported on the discharging port of the discharging hopper, a discharging support member arranged on the inner side of the discharging pipe, a transmission shaft installed on the discharging support member, and a discharging spiral arranged on the outer side of the transmission shaft; the transmission shaft extends upward through the discharging port and is connected to the arch breaking assembly.
7. The fumed silica powder silo according to claim 6, characterized in that: One end of the rotating shaft adjacent to the transmission shaft is connected to the transmission shaft through a coupling, and the other end of the rotating shaft away from the transmission shaft is rotatably mounted on the intermediate support member through a bearing.
8. The fumed silica powder silo according to claim 7, characterized in that: The intermediate support member includes a ring body mounted on the inner side of the tank body, and a plurality of supporting ribs provided on the inner side of the ring body.
9. The fumed silica powder silo according to claim 1, characterized in that: The plurality of first arch-breaking members are staggeredly distributed along the axial direction of the rotating shaft; each of the plurality of first arch-breaking members comprises a screw rod mounted on the rotating shaft, and a single-sided blade mounted on one end of the screw rod away from the rotating shaft.
10. The fumed silica powder silo according to claim 1, characterized in that: The second arch-breaking member is C-shaped; two second arch-breaking members are arranged on the rotating shaft, and the two second arch-breaking members are arranged opposite to each other along the radial direction of the rotating shaft.
Citation Information
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