CN106422914B - Centrifugal powder particle mixing device - Google Patents
Centrifugal powder particle mixing device Download PDFInfo
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- CN106422914B CN106422914B CN201611119416.0A CN201611119416A CN106422914B CN 106422914 B CN106422914 B CN 106422914B CN 201611119416 A CN201611119416 A CN 201611119416A CN 106422914 B CN106422914 B CN 106422914B
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- 239000000843 powder Substances 0.000 title claims abstract description 94
- 239000002245 particle Substances 0.000 title claims description 8
- 239000013078 crystal Substances 0.000 claims abstract description 5
- 230000000903 blocking effect Effects 0.000 claims description 44
- 239000000203 mixture Substances 0.000 abstract description 7
- 238000012824 chemical production Methods 0.000 abstract description 3
- 239000004744 fabric Substances 0.000 abstract 4
- 235000017166 Bambusa arundinacea Nutrition 0.000 abstract 3
- 235000017491 Bambusa tulda Nutrition 0.000 abstract 3
- 241001330002 Bambuseae Species 0.000 abstract 3
- 235000015334 Phyllostachys viridis Nutrition 0.000 abstract 3
- 239000011425 bamboo Substances 0.000 abstract 3
- 239000011812 mixed powder Substances 0.000 abstract 1
- 238000000034 method Methods 0.000 description 5
- 230000009471 action Effects 0.000 description 4
- 230000008569 process Effects 0.000 description 4
- 238000005096 rolling process Methods 0.000 description 3
- 238000005054 agglomeration Methods 0.000 description 2
- 230000002776 aggregation Effects 0.000 description 2
- 230000008878 coupling Effects 0.000 description 2
- 238000010168 coupling process Methods 0.000 description 2
- 238000005859 coupling reaction Methods 0.000 description 2
- 238000010586 diagram Methods 0.000 description 2
- 230000005484 gravity Effects 0.000 description 2
- 239000000126 substance Substances 0.000 description 2
- 238000005299 abrasion Methods 0.000 description 1
- 230000009286 beneficial effect Effects 0.000 description 1
- 230000008859 change Effects 0.000 description 1
- 238000002474 experimental method Methods 0.000 description 1
- 239000000463 material Substances 0.000 description 1
- 230000005012 migration Effects 0.000 description 1
- 238000013508 migration Methods 0.000 description 1
- 230000001105 regulatory effect Effects 0.000 description 1
- 238000000926 separation method Methods 0.000 description 1
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Classifications
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- B—PERFORMING OPERATIONS; TRANSPORTING
- B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
- B01F—MIXING, e.g. DISSOLVING, EMULSIFYING OR DISPERSING
- B01F29/00—Mixers with rotating receptacles
- B01F29/80—Mixers with rotating receptacles rotating about a substantially vertical axis
- B01F29/81—Mixers with rotating receptacles rotating about a substantially vertical axis with stationary mixing elements
-
- B—PERFORMING OPERATIONS; TRANSPORTING
- B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
- B01F—MIXING, e.g. DISSOLVING, EMULSIFYING OR DISPERSING
- B01F23/00—Mixing according to the phases to be mixed, e.g. dispersing or emulsifying
- B01F23/60—Mixing solids with solids
-
- B—PERFORMING OPERATIONS; TRANSPORTING
- B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
- B01F—MIXING, e.g. DISSOLVING, EMULSIFYING OR DISPERSING
- B01F29/00—Mixers with rotating receptacles
- B01F29/15—Use of centrifuges for mixing
-
- B—PERFORMING OPERATIONS; TRANSPORTING
- B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
- B01F—MIXING, e.g. DISSOLVING, EMULSIFYING OR DISPERSING
- B01F29/00—Mixers with rotating receptacles
- B01F29/40—Parts or components, e.g. receptacles, feeding or discharging means
- B01F29/403—Disposition of the rotor axis
- B01F29/4032—Disposition of the rotor axis vertical
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- Chemical & Material Sciences (AREA)
- Chemical Kinetics & Catalysis (AREA)
- Crushing And Grinding (AREA)
- Mixers Of The Rotary Stirring Type (AREA)
Abstract
Description
技术领域technical field
本发明设计到一种分离混合装置,具体涉及到一种在固定容器内具有旋转装置的粉粒混合装置。The present invention is designed to a separation mixing device, in particular to a powder mixing device with a rotating device in a fixed container.
背景技术Background technique
粉粒的混合在化学实验和化工生产过程经常遇到,混合的最终目的是在混合均匀的基础上,确保混合物的性质不发生改变,物质间不能发生反应,因此混合过程应该尽量避免对粉粒的高强度碾压。比如,实验室进行有机物晶体混合时,如果混合过程中出现碾压,很可能导致晶体的结构改变。此外,密度差异大的物质难以一次性混合均匀,而多次混合需要对现有装置进行拆卸和重新装料,步骤繁琐。The mixing of powder particles is often encountered in chemical experiments and chemical production processes. The ultimate purpose of mixing is to ensure that the properties of the mixture do not change and the substances cannot react on the basis of uniform mixing. Therefore, the mixing process should try to avoid the powder particles. high-strength rolling. For example, when mixing organic crystals in the laboratory, if there is rolling during the mixing process, it is likely to cause changes in the structure of the crystals. In addition, it is difficult to mix materials with large differences in density evenly at one time, and the existing device needs to be disassembled and recharged for multiple mixing, which is a cumbersome process.
发明内容SUMMARY OF THE INVENTION
本发明所要解决的技术问题在于克服现有粉粒混合装置的缺点,提供一种设计合理、混合均匀、操作简单、对粉粒磨损小的离心式粉粒混合装置。The technical problem to be solved by the present invention is to overcome the shortcomings of the existing powder mixing device, and provide a centrifugal powder mixing device with reasonable design, uniform mixing, simple operation and little abrasion to the powder.
解决上述技术问题所采用的技术方案是:在底座中部设置有电机,电机的动力输出轴上设置有混粉槽,混粉槽内由下向上依次设置有下筛网、上筛网、挡筒,下筛网和上筛网以及挡筒的中心加工有孔径相同的孔,挡筒与混粉槽壁之间有狭缝,混粉槽上设置有混粉槽盖,混粉槽盖外表面中心设置有与混粉槽盖连为一体短轴,底座上设置有支撑杆,支撑杆上设置有定位圆盘,定位圆盘的中部设置有与短轴相匹配的凹槽。The technical solution adopted to solve the above technical problems is as follows: a motor is arranged in the middle of the base, a powder mixing tank is arranged on the power output shaft of the motor, and a lower screen, an upper screen and a blocking cylinder are arranged in the powder mixing tank from bottom to top. , the center of the lower screen, the upper screen and the blocking cylinder are machined with holes with the same diameter, there is a slit between the blocking cylinder and the wall of the mixing tank, the mixing tank is provided with a mixing tank cover, and the outer surface of the mixing tank cover is The center is provided with a short shaft connected with the powder mixing tank cover, the base is provided with a support rod, the support rod is provided with a positioning disc, and the middle of the positioning disc is provided with a groove matching the short shaft.
本发明的混粉槽的结构是倒锥形筒与外凸球面底连为一体,混粉槽倒锥形筒的母线与轴线的夹角为25°~45°,混粉槽倒锥形筒大口径与小口径比值为1.5~3。The structure of the powder mixing tank of the present invention is that the inverted conical cylinder and the outer convex spherical bottom are connected as a whole, the included angle between the generatrix and the axis of the inverted conical cylinder of the powder mixing tank is 25° to 45°, and the inverted conical cylinder of the powder mixing tank is integrated. The ratio of large caliber to small caliber is 1.5 to 3.
本发明的挡筒呈圆锥筒状,在挡筒的小端口外侧设置有小挡环,小挡环的中心 线与挡筒的中心线重合,挡筒倒置在混粉槽内,小挡环抵在上筛网上,挡筒大端口外侧设置有沿圆周方向均匀分布的固定板条,挡筒通过固定板条固定在混粉槽内壁上。The blocking cylinder of the present invention is in the shape of a conical cylinder, and a small blocking ring is arranged outside the small port of the blocking cylinder. The center line of the small blocking ring coincides with the center line of the blocking cylinder. On the upper screen, fixed slats evenly distributed along the circumferential direction are arranged on the outside of the large port of the blocking cylinder, and the blocking cylinder is fixed on the inner wall of the powder mixing tank through the fixed slats.
本发明的上筛网为环形平面网。The upper screen mesh of the present invention is an annular plane mesh.
本发明的下筛网为锥形筒状网,下筛网大端口在下小端口在上设置在混粉槽内底部,下筛网的大端口直径与混粉槽倒锥形筒小端口直径相同,下筛网的高度等于上筛网距混粉槽底面的高度,下筛网的小端口直径与挡筒小端口径和上筛网的中心孔孔径相同。The lower screen of the present invention is a conical cylindrical screen, the large port of the lower screen is set at the bottom of the powder mixing tank on top of the lower small port, and the diameter of the large port of the lower screen is the same as the diameter of the small port of the inverted conical cylinder of the powder mixing tank. , the height of the lower screen is equal to the height of the upper screen from the bottom surface of the mixing tank, and the diameter of the small port of the lower screen is the same as the diameter of the small port of the baffle and the central hole of the upper screen.
本发明的挡筒母线与轴线之间的夹角为35°~55°,挡筒大端面的直径与小端面的直径比为1.5~3。The angle between the generatrix of the blocking cylinder and the axis of the invention is 35°˜55°, and the ratio of the diameter of the large end face of the blocking cylinder to the diameter of the small end face is 1.5˜3.
本发明的下筛网母线与轴线的夹角为45°~65°。The included angle between the bus bar of the lower screen mesh and the axis of the present invention is 45°-65°.
本发明的下筛网和上筛网的网孔直径为2~5mm。The mesh diameter of the lower screen and the upper screen of the present invention is 2-5 mm.
本发明的有益效果如下:The beneficial effects of the present invention are as follows:
本发明电机的动力输出轴上通过联轴器连接有混粉槽,混粉槽内由下向上设置有下筛网和上筛网,电机带动混粉槽转动,混粉槽内不同的粉末在离心力的作用下,依次穿过下筛网和上筛网,下筛网用于粉碎粉末结块,上筛网用于二次粉碎粉末结块,上升过程中较大密度的粉粒受到的离心力较大,同时受到的重力阻力也大,两者相互抵消,可实现不同密度粉粒的同速移动;粉末转移至混粉槽顶端后,停止电机旋转,粉粒则会在重力作用下返回混粉槽底部,通过启动-停止电机的反复操作可方便粉末的多次混合;粉末迁移由离心力驱动,避免了高强度的撞击和碾压,本发明操作简单、成本低,对粉末晶体的损伤小,混合效率高,在化工生产领域可广泛推广使用。The power output shaft of the motor of the present invention is connected with a powder mixing tank through a coupling, a lower screen and an upper screen are arranged in the powder mixing tank from bottom to top, the motor drives the powder mixing tank to rotate, and different powders in the powder mixing tank are Under the action of centrifugal force, it passes through the lower screen and the upper screen in turn. The lower screen is used to pulverize powder agglomerates, and the upper screen is used for secondary powder agglomeration. At the same time, the gravitational resistance is also large. The two cancel each other out, and the powder particles of different densities can move at the same speed; after the powder is transferred to the top of the mixing tank, stop the motor rotation, and the powder particles will return to the mixing under the action of gravity. At the bottom of the powder tank, repeated operations of starting and stopping the motor can facilitate the multiple mixing of powder; powder migration is driven by centrifugal force, avoiding high-strength impact and rolling, and the invention has simple operation, low cost, and little damage to powder crystals , high mixing efficiency, can be widely used in the field of chemical production.
附图说明Description of drawings
图1是本发明的结构示意图。Figure 1 is a schematic structural diagram of the present invention.
图2是图1中挡筒5的结构示意图。FIG. 2 is a schematic structural diagram of the blocking
图3是图2的A-A剖视图。FIG. 3 is a cross-sectional view taken along line A-A of FIG. 2 .
具体实施方式Detailed ways
下面结合附图和实施例对本发明进一步详细说明,但本发明不限于下述的实施方式。The present invention will be further described in detail below with reference to the accompanying drawings and examples, but the present invention is not limited to the following embodiments.
在图1、2、3中,本实施例的离心式粉粒混合装置由底座10、电机9、混粉槽4、下筛网7、上筛网6、挡筒5、混粉槽盖3、短轴2、支撑杆8、定位圆盘1连接构成。In Figures 1, 2 and 3, the centrifugal powder mixing device of this embodiment consists of a
在底座10中部安装有电机9,电机9为调速电机9,电机9的动力输出轴上通过联轴器连接有混粉槽4,混粉槽4是倒锥形筒与外凸球面底连为一体,混粉槽母线与轴线的夹角为35°,混粉槽4的倒锥形筒的大口径与小口径比值为2,混粉槽4内由下向上依次设置有下筛网7、上筛网6、挡筒5,下筛网7和上筛网6以及挡筒5的中心线与混粉槽4的中心线重合,下筛网7为锥形筒状网,下筛网7母线与轴线的夹角为55°,下筛网7大端口在下小端口在上放置在混粉槽4内底部,下筛网7的大端口直径与混粉槽倒锥形筒小端口直径相同,下筛网7的高度等于上筛网6距混粉槽4底面的高度,下筛网7用于粉碎粉末结块,上筛网6为环形平面网,上筛网用于二次粉碎粉末结块,使不同的粉末混合充分,上筛网6的中心孔孔径与下筛网7小端口直径相等,下筛网7和上筛网6的网孔直径为3mm,挡筒5呈圆锥筒状,挡筒5母线与轴线之间的夹角为45°,挡筒5大端面的直径与小端面的直径比为2,挡筒5的小端口直径与下筛网7小端口直径相等,在挡筒5的小端口外侧设置有小挡环5-3,小挡环5-3的中心线与挡筒5的中心线重合,挡筒5小端口在下大端口向上放置在混粉槽4内,小挡环5-3抵在上筛网6上,挡筒5大端口外侧设置有沿圆周方向均匀分布的固定板条5-2,挡筒5通过固定板条5-2固定在混粉槽内壁上,使挡筒5大端口边沿与混粉槽内壁留有狭缝,混粉槽4上通过螺纹连接 有混粉槽盖3,混粉槽盖3外表面中心设置有与混粉槽盖3连为一体短轴2,短轴2的端部伸入到定位圆盘1的凹槽内,定位圆盘1通过支撑杆8固定在底座10上。A
使用时,打开混粉槽盖3,倒入需要混合的粉末,将混粉槽盖3旋拧在混粉槽口上,封闭混粉槽,启动电机9,电机9转动带动混粉槽转动,粉末将在离心力的作用下依次穿过下筛网和上筛网以及挡筒狭缝转移至混粉槽的顶部,停止电机9旋转,粉粒则会在重力作用下通过导筒端口重新回到混粉槽底部,如此反复操作可实现粉末多次混合均匀。When in use, open the powder mixing
实施例2Example 2
在本实施例中,混粉槽4的结构是倒锥形筒与外凸球面底连为一体,混粉槽4倒锥形筒的母线与轴线的夹角为25°,混粉槽4倒锥形筒大口径与小口径比值为1.5,混粉槽4内由下向上依次设置有下筛网7、上筛网6、挡筒5,下筛网7母线与轴线的夹角为45°,挡筒5母线与轴线之间的夹角为35°,挡筒5大端面的直径与小端面的直径比为1.5,所述的下筛网7和上筛网6的网孔直径为2mm。In this embodiment, the structure of the
其他零部件及零部件的连接关系与实施例1相同。The other parts and the connection relationship of the parts are the same as those in the first embodiment.
实施例3Example 3
在本实施例中,混粉槽4的结构是倒锥形筒与外凸球面底连为一体,混粉槽4倒锥形筒的母线与轴线的夹角为45°,混粉槽4倒锥形筒大口径与小口径比值为3,混粉槽4内由下向上依次设置有下筛网7、上筛网6、挡筒5,下筛网7母线与轴线的夹角为65°,挡筒5母线与轴线之间的夹角为55°,挡筒5大端面的直径与小端面的直径比为3,所述的下筛网7和上筛网6的网孔直径为5mm。其他零部件及零部件的连接关系与实施例1相同。In this embodiment, the structure of the
Claims (8)
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| CN110057899B (en) * | 2019-04-14 | 2022-01-28 | 北京工业大学 | System and method for characterizing molecular structure of extracellular polymer of anaerobic ammonia oxidation sludge |
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| GB1482006A (en) * | 1973-11-19 | 1977-08-03 | Acme Cleveland Corp | Foundry mixing machine |
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| IT1024318B (en) * | 1973-11-14 | 1978-06-20 | Dillumelt Srl | PROCESS FOR MESOOLAR IN A TINUOUS WAY A POWDER IN A LIQUID AND DEVICE FOR STARTING THE PROCESS |
| CN2472624Y (en) * | 2001-04-12 | 2002-01-23 | 广东天际电器有限公司 | Household food stirrer |
| CN2614786Y (en) * | 2003-02-28 | 2004-05-12 | 王化栋 | Shaft top gear disc crushing automatic separator |
| CN202700427U (en) * | 2012-07-04 | 2013-01-30 | 深圳市尚水智能设备有限公司 | Scattering device |
| CN103657491B (en) * | 2013-12-04 | 2015-08-26 | 上海森松混合技术工程装备有限公司 | A kind of Squirrel-cage type supergravity mixer |
| CN104647589B (en) * | 2015-01-26 | 2016-08-24 | 中国矿业大学 | A kind of vertical pulper of mining fire extinguishing |
| CN204518450U (en) * | 2015-03-10 | 2015-08-05 | 邯郸市成通灌溉节能设备有限公司 | Injection moulding pressure differential tank |
| CN204735166U (en) * | 2015-06-30 | 2015-11-04 | 何淑琼 | Centrifugal blender |
| CN206295886U (en) * | 2016-12-08 | 2017-07-04 | 西北大学 | Centrifugal powder mixing arrangement |
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| GB1482006A (en) * | 1973-11-19 | 1977-08-03 | Acme Cleveland Corp | Foundry mixing machine |
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