CN221156247U - PTA refining crystallization kettle stirrer - Google Patents
PTA refining crystallization kettle stirrer Download PDFInfo
- Publication number
- CN221156247U CN221156247U CN202322879271.6U CN202322879271U CN221156247U CN 221156247 U CN221156247 U CN 221156247U CN 202322879271 U CN202322879271 U CN 202322879271U CN 221156247 U CN221156247 U CN 221156247U
- Authority
- CN
- China
- Prior art keywords
- stirring shaft
- blade
- kettle body
- hub
- kettle
- Prior art date
- Legal status (The legal status is an assumption and is not a legal conclusion. Google has not performed a legal analysis and makes no representation as to the accuracy of the status listed.)
- Active
Links
- 238000002425 crystallisation Methods 0.000 title claims abstract description 16
- 230000008025 crystallization Effects 0.000 title claims abstract description 16
- 238000007670 refining Methods 0.000 title claims abstract description 12
- 238000003756 stirring Methods 0.000 claims abstract description 54
- 239000003638 chemical reducing agent Substances 0.000 claims description 10
- 238000007789 sealing Methods 0.000 claims description 7
- 230000005540 biological transmission Effects 0.000 claims description 6
- 210000004907 gland Anatomy 0.000 claims description 6
- 230000008878 coupling Effects 0.000 claims 1
- 238000010168 coupling process Methods 0.000 claims 1
- 238000005859 coupling reaction Methods 0.000 claims 1
- 238000000034 method Methods 0.000 abstract description 9
- 239000002245 particle Substances 0.000 abstract description 8
- 230000000694 effects Effects 0.000 abstract description 6
- 239000000463 material Substances 0.000 abstract description 5
- 238000001556 precipitation Methods 0.000 abstract description 4
- 239000007787 solid Substances 0.000 abstract description 4
- 239000000725 suspension Substances 0.000 abstract description 4
- 238000002360 preparation method Methods 0.000 abstract description 2
- 239000007788 liquid Substances 0.000 description 12
- 230000006378 damage Effects 0.000 description 3
- 239000013590 bulk material Substances 0.000 description 2
- 238000001125 extrusion Methods 0.000 description 2
- 238000002156 mixing Methods 0.000 description 2
- 238000012986 modification Methods 0.000 description 2
- 230000004048 modification Effects 0.000 description 2
- 239000013618 particulate matter Substances 0.000 description 2
- 238000005086 pumping Methods 0.000 description 2
- 238000005452 bending Methods 0.000 description 1
- 230000007547 defect Effects 0.000 description 1
- 238000013461 design Methods 0.000 description 1
- 239000000945 filler Substances 0.000 description 1
- 230000003993 interaction Effects 0.000 description 1
- 238000012423 maintenance Methods 0.000 description 1
- 238000005259 measurement Methods 0.000 description 1
- 230000001360 synchronised effect Effects 0.000 description 1
- 238000003466 welding Methods 0.000 description 1
Landscapes
- Mixers Of The Rotary Stirring Type (AREA)
Abstract
The utility model relates to the technical field of PTA preparation, in particular to a PTA refined crystallization kettle stirrer, which comprises a kettle body and a stirring shaft, wherein the kettle body is arranged on a frame, the stirring shaft extends from the bottom of the kettle body to the inside of the kettle body, a hub is arranged at the end part of the stirring shaft in the kettle body, the hub is of a hollow cylindrical structure, a plurality of lugs are arranged on the circumferential outer surface of the hub at intervals, a blade is fixed on each lug through a connecting bolt, an included angle is formed between the blade and a vertical plane, and the angle at the upper end of the outer side of the blade is bent downwards. According to the PTA refining crystallization kettle stirrer, an included angle is formed between the blade and the vertical plane through the inclined arrangement of the lug plates, and meanwhile, the upper end of the outer side of the blade is bent downwards, so that the axial acting force on materials in the rotation process of the blade can be effectively increased, the precipitation of solid particles is avoided, the suspension state of the fixed body particles is good, and the stirring effect is better.
Description
Technical Field
The utility model relates to the technical field of PTA preparation, in particular to a PTA refining crystallization kettle stirrer.
Background
The stirrer adopted by the PTA refining crystallization kettle at present is generally an axial flow paddle, and the stirring of the axial flow paddle in the stirrer can solve the following problems: the stirrer is easy to damage, and solid precipitation is easy to occur in the crystallization kettle. Specifically: the damage of the stirrer mainly comprises blade deformation, bending of a stirring shaft and the like; the occurrence of solid precipitation is mainly that stirring particle suspension effect is poor, a large amount of fixed particle deposit, and particle deposit is in (mixing) shaft and cauldron body sealing department, and the clearance is wasted time and energy when later maintenance, also can cause the material extravagant.
It is necessary to design a stirrer for the PTA refining crystallization kettle.
Disclosure of utility model
The utility model aims to solve the technical defects and provides the PTA refining crystallization kettle stirrer which can improve the flow rate of suspended particles in the stirring process, is not easy to precipitate and simultaneously generates larger stirring acting force in the axial direction.
The utility model discloses a PTA refining crystallization kettle stirrer, which comprises a kettle body and a stirring shaft, wherein the kettle body is arranged on a frame, a motor and a speed reducer are arranged on the frame, the motor is in transmission connection with the speed reducer, and the speed reducer is in transmission connection with the stirring shaft through a coupler; the stirring shaft extends to the inside of the kettle body from the bottom of the kettle body, a hub is arranged at the end part of the stirring shaft in the kettle body, the hub is of a hollow cylindrical structure, a plurality of lugs are arranged on the circumferential outer surface of the hub at intervals, a blade is fixed on each lug through a connecting bolt, the blade forms an included angle with a vertical plane, and the angle at the upper end of the outer side of the blade is bent downwards.
The hub is sleeved at the end part of the stirring shaft and is fixed through the gland and the locking bolt.
The stirring shaft is provided with a stirring shaft, a stirring shaft is arranged on the stirring shaft, a stirring flange is arranged on the rack, an equipment flange is arranged at the bottom of the kettle body, the equipment flange is connected with the mounting flange in a matched mode, and the stirring shaft penetrates through the equipment flange and the mounting flange and is connected with the stirring shaft in a sealing mode.
According to the PTA refining crystallization kettle stirrer, an included angle is formed between the blade and the vertical plane through the inclined arrangement of the lug plates, and meanwhile, the upper end of the outer side of the blade is bent downwards, so that the axial acting force on materials in the rotation process of the blade can be effectively increased, the precipitation of solid particles is avoided, the suspension state of the fixed body particles is good, and the stirring effect is better.
Drawings
Fig. 1 is a schematic structural view of the present utility model.
Detailed Description
In order to further describe the technical means and effects adopted by the present utility model for achieving the intended purpose, the following detailed description will refer to the specific implementation, structure, characteristics and effects according to the present utility model with reference to the accompanying drawings and preferred embodiments.
Example 1:
As shown in fig. 1, the utility model discloses a PTA refined crystallization kettle stirrer, which comprises a kettle body 1 and a stirring shaft 3, wherein the kettle body 1 is arranged on a frame 2, a motor 4 and a speed reducer 5 are arranged on the frame 2, the motor 4 is in transmission connection with the speed reducer 5, and the speed reducer 5 is in transmission connection with the stirring shaft 3 through a coupler 6; the stirring shaft 3 extends to the inside of the kettle body 1 from the bottom of the kettle body 1, a hub 7 is arranged at the end part of the stirring shaft 3 inside the kettle body 1, the hub 7 is of a hollow cylindrical structure, a plurality of lugs 8 are arranged on the circumferential outer surface of the hub 7 at intervals, a blade 9 is fixed on each lug 8 through a connecting bolt, the blade 9 forms an included angle with a vertical plane, and the angle at the upper end of the outer side of the blade 9 is bent downwards.
The end part of the stirring shaft 3 is sleeved with a hub 7, an ear plate 8 on the hub 7 is connected through welding, a certain included angle exists between the ear plate 8 and a vertical plane, and under normal conditions, the upper end of the ear plate 8 is positioned in front of the rotation direction of the stirring shaft 3. The whole blade 9 is flat, so that an included angle is formed between the whole blade 9 and the vertical plane. The angle of the upper end of the outer side of the blade 9 is bent downwards, so that the angle between the part of the upper end of the outer side of the blade 9 and the vertical plane is slightly larger than the angle between the whole blade 9 and the vertical plane. The paddle 9 of this kind of form is under motor 4 and the drive of speed reducer 5, realize stirring the inside liquid of cauldron body 1, and stirring in-process liquid can receive radial effort and two parts axial decurrent effort, and the size of two parts axial effort is different, and liquid can the undercut extrusion in the stirring process to make the liquid of (mixing) shaft 3 bottom can receive the extrusion, outwards circulate along cauldron body 1 diapire, finally let the liquid in the cauldron body 1 realize radial, axial synchronous circulation stirring, can effectively avoid the particulate matter in the liquid to deposit in the bottom of the cauldron body 1, the mobility of liquid in the cauldron body 1 is better, and relate to each position, promoted the stirring effect to the liquid.
The stirrer of above-mentioned scheme can promote the axial pumping capacity in the stirring process, has promoted the suspension ability of liquid particulate matter, simultaneously, and the stirrer provides comprehensive axial and radial pumping capacity, can promote the liquid velocity of flow, and the knot wall material on the inner wall of the cauldron body 1 in the PTA crystallization process is continuously erodeed, avoids the material to pile up constantly and produces the bulk material, so can reduce the bulk material and drop and cause the condition emergence of destruction to paddle 9.
The hub 7 is sleeved at the end part of the stirring shaft 3 and is fixed through the gland 10 and the locking bolt 11. Since the paddle 9 generates an axial downward force on the liquid in the rotation process, the liquid generates an axial upward force on the paddle 9, so that the gland 10 and the locking bolt 11 are adopted to fix the hub 7 on the end part of the stirring shaft 3, the gland 10 can be fixed on the end part of the stirring shaft 3 by the locking bolt 11, and the gland 10 can limit the hub 7 on the stirring shaft 3 to avoid falling off due to external force.
The stirring shaft 3 passes through the equipment flange 12 and the mounting flange 13, and the equipment flange 12 is in sealing connection with the stirring shaft 3.
The frame 2 is connected with the kettle body 1 through the mounting flange 13 and the equipment flange 12, and the connection is simple and convenient, firm and stable. The stirring shaft 3 and the equipment flange 12 are sealed, and the sealing can be realized by adopting filler sealing, so that the stirring shaft 3 is always sealed with the equipment flange 12 in the rotating process, and the sealing performance is good.
According to the technical scheme, the actual measurement data are as follows: 1. shaft power under normal conditions: 60kw;2. leaf tip linear velocity: 5.42m/s;3. apparent flow rate: 0.36m/s;4. number of tumbling: 5.8 times/min.
In the description of the present application, it should be understood that the terms "center", "longitudinal", "lateral", "length", "width", "thickness", "upper", "lower", "front", "rear", "left", "right", "vertical", "horizontal", "top", "bottom", "inner", "outer", "clockwise", "counterclockwise", etc. indicate orientations or positional relationships based on the orientations or positional relationships shown in the drawings are merely for convenience in describing the present application and simplifying the description, and do not indicate or imply that the device or element referred to must have a specific orientation, be configured and operated in a specific orientation, and thus should not be construed as limiting the present application. Furthermore, the terms "first," "second," and the like, are used for descriptive purposes only and are not to be construed as indicating or implying a relative importance or implicitly indicating the number of technical features indicated. Thus, a feature defining "a first" or "a second" may explicitly or implicitly include one or more such feature. In the description of the present application, the meaning of "a plurality" is two or more, unless explicitly defined otherwise.
In the description of the present application, it should be noted that, unless explicitly specified and limited otherwise, the terms "mounted," "connected," and "connected" are to be construed broadly, and may be either fixedly connected, detachably connected, or integrally connected, for example; may be a mechanical connection; can be directly connected or indirectly connected through an intermediate medium, and can be in interaction relationship with two elements. The specific meaning of the above terms in the present application can be understood by those of ordinary skill in the art according to the specific circumstances.
In the present application, unless expressly stated or limited otherwise, a first feature "above" or "below" a second feature may include both the first and second features being in direct contact, as well as the first and second features not being in direct contact but being in contact with each other through additional features therebetween. Moreover, a first feature being "above," "over" and "on" a second feature includes the first feature being directly above and obliquely above the second feature, or simply indicating that the first feature is higher in level than the second feature. The first feature being "under", "below" and "beneath" the second feature includes the first feature being directly under and obliquely below the second feature, or simply means that the first feature is less level than the second feature.
The present utility model is not limited to the preferred embodiments, but is capable of modification and variation in detail, and other modifications and variations can be made by those skilled in the art without departing from the scope of the present utility model.
Claims (3)
1. The PTA refining crystallization kettle stirrer comprises a kettle body and a stirring shaft, and is characterized in that: the kettle body is arranged on the frame, a motor and a speed reducer are arranged on the frame, the motor is in transmission connection with the speed reducer, and the speed reducer is in transmission connection with the stirring shaft through a coupling; the stirring shaft extends to the inside of the kettle body from the bottom of the kettle body, a hub is arranged at the end part of the stirring shaft in the kettle body, the hub is of a hollow cylindrical structure, a plurality of lugs are arranged on the circumferential outer surface of the hub at intervals, a blade is fixed on each lug through a connecting bolt, the blade forms an included angle with a vertical plane, and the angle at the upper end of the outer side of the blade is bent downwards.
2. The PTA refining crystallization kettle stirrer according to claim 1, wherein: the hub is sleeved at the end part of the stirring shaft and is fixed through the gland and the locking bolt.
3. The PTA refining crystallization kettle stirrer according to claim 1, wherein: the stirring shaft is provided with a stirring shaft, a stirring shaft is arranged on the stirring shaft, a stirring flange is arranged on the rack, an equipment flange is arranged at the bottom of the kettle body, the equipment flange is connected with the mounting flange in a matched mode, and the stirring shaft penetrates through the equipment flange and the mounting flange and is connected with the stirring shaft in a sealing mode.
Priority Applications (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
CN202322879271.6U CN221156247U (en) | 2023-10-25 | 2023-10-25 | PTA refining crystallization kettle stirrer |
Applications Claiming Priority (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
CN202322879271.6U CN221156247U (en) | 2023-10-25 | 2023-10-25 | PTA refining crystallization kettle stirrer |
Publications (1)
Publication Number | Publication Date |
---|---|
CN221156247U true CN221156247U (en) | 2024-06-18 |
Family
ID=91532252
Family Applications (1)
Application Number | Title | Priority Date | Filing Date |
---|---|---|---|
CN202322879271.6U Active CN221156247U (en) | 2023-10-25 | 2023-10-25 | PTA refining crystallization kettle stirrer |
Country Status (1)
Country | Link |
---|---|
CN (1) | CN221156247U (en) |
-
2023
- 2023-10-25 CN CN202322879271.6U patent/CN221156247U/en active Active
Similar Documents
Publication | Publication Date | Title |
---|---|---|
CN210079341U (en) | Dispersion devices is used in graphite alkene processing | |
CN221156247U (en) | PTA refining crystallization kettle stirrer | |
CN204891280U (en) | Swept -back wing frame type stirrer crystallization equipment | |
CN211659848U (en) | High-speed shear type stirring device | |
CN218249658U (en) | Stirring device | |
CN209155732U (en) | Vertical flocculation stirring device | |
CN215311776U (en) | Insoluble felt binder agitating unit | |
CN216094125U (en) | High-speed pulping machine | |
JP4635149B2 (en) | Stirrer | |
CN112619465A (en) | Stirring rake and agitator | |
CN217248394U (en) | Slurry stirring device for production of covering slag | |
CN206463865U (en) | A kind of new die bond solder paste agitator | |
CN216799427U (en) | Take fan-shaped air supporting flocculation mixer of spiral | |
CN212790769U (en) | Agricultural feed stirring device | |
CN219502620U (en) | Seasoning powder mixing tank | |
CN218077328U (en) | Novel stirring paddle | |
CN219505101U (en) | Concrete mixing device for building construction | |
CN214293710U (en) | Environment-friendly mud liquid agitating unit | |
CN217221032U (en) | High-efficient mud mixer | |
CN211837511U (en) | Coating stirring device | |
CN211677465U (en) | Agricultural agitating unit convenient to fertilizer mixes | |
CN217663226U (en) | A material reaction unit for phosphoric acid production | |
CN215877431U (en) | Cement grinding aid feeding and mixing device | |
CN219518432U (en) | Auxiliary agent liquid material agitated vessel | |
CN220047966U (en) | Nanometer additive preparation blending device |
Legal Events
Date | Code | Title | Description |
---|---|---|---|
GR01 | Patent grant | ||
GR01 | Patent grant |