TWI677375B - Agglomerated powder dispersion device - Google Patents
Agglomerated powder dispersion device Download PDFInfo
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- TWI677375B TWI677375B TW107134223A TW107134223A TWI677375B TW I677375 B TWI677375 B TW I677375B TW 107134223 A TW107134223 A TW 107134223A TW 107134223 A TW107134223 A TW 107134223A TW I677375 B TWI677375 B TW I677375B
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Abstract
一種凝聚粉體分散裝置,包括噴嘴、基座與衝擊球,噴嘴與基座內部分別具有進氣道與出氣道,對接後形成衝擊室並與進氣道、出氣道相互連通,衝擊球固定於夾持片上並安置於衝擊室內,凝聚粉體隨氣流由進氣道進入衝擊室衝向衝擊球表面,經衝擊分散後的粉體再由出氣道排出。A condensed powder dispersion device includes a nozzle, a base, and an impact ball. The nozzle and the base respectively have an air inlet and an air outlet. After being connected, an impact chamber is formed and communicates with the air inlet and the air outlet. The impact ball is fixed on the The clamping piece is placed on the impact chamber, and the condensed powder enters the impact chamber with the airflow and rushes to the surface of the impact ball. The powder dispersed after impact is discharged through the air outlet.
Description
本發明是有關於一種分散裝置,且特別是有關於一種藉由慣性衝擊方式使凝聚的粉體分散之裝置。The present invention relates to a dispersing device, and more particularly, to a device for dispersing agglomerated powder by an inertial impact method.
微細粉體之間常因為凡德瓦力、靜電、水分附著於表面之張力等而發生物理性的凝聚或結塊的現象,特別是粒徑越小而表面積與體積比例越大之粉體更是明顯,這對於工業使用上將造成困擾與不便。The physical condensation or agglomeration of fine powders often occurs due to van der Waals force, static electricity, and the tension of moisture attached to the surface. Especially, the smaller the particle size, the larger the surface area to volume ratio. It is obvious that this will cause distress and inconvenience to industrial use.
目前為使凝聚粉體分散之方式有振盪法,利用外力對粉體施予振盪,以振盪之能量克服粉體之間的交互作用力以進行分散。另一方式為化學法,外加某化合物與凝聚粉體產生化學反應而先成為中間產物,再另以某程序將反應後的產物還原回原粉體。The current method for dispersing the agglomerated powder is the oscillation method, which uses external force to oscillate the powder, and uses the energy of the oscillation to overcome the interaction force between the powders for dispersion. The other method is a chemical method, in which a chemical compound reacts with the agglomerated powder to become an intermediate product, and then the reaction product is reduced back to the original powder by a certain procedure.
本發明有關於一種凝聚粉體分散裝置,包括噴嘴、基座與衝擊球,噴嘴與基座內部分別具有進氣道與出氣道,對接後形成衝擊室並與進氣道、出氣道相互連通,衝擊球固定於夾持片上並安置於衝擊室內,凝聚粉體隨氣流由進氣道進入衝擊室衝向衝擊球表面,經衝擊分散後的粉體再由出氣道排出。The invention relates to a condensed powder dispersion device, which includes a nozzle, a base and an impact ball. The nozzle and the base respectively have an air inlet channel and an air outlet channel. After docking, an impact chamber is formed and communicates with the air inlet channel and the air outlet channel. The impact ball is fixed on the clamping piece and is placed in the impact chamber. The condensed powder enters the impact chamber from the air inlet and rushes to the surface of the impact ball. The powder dispersed after impact is discharged through the air outlet.
為了對本發明之上述及其他方面有更佳的瞭解,下文特舉實施例,並配合所附圖式詳細說明如下:In order to have a better understanding of the above and other aspects of the present invention, the following specific examples are described in detail below in conjunction with the accompanying drawings:
以下提出實施例進行詳細說明,惟實施例僅用以作為範例說明,並非用以限縮本發明保護之範圍。以下是以相同或類似的符號表示相同或類似的元件做說明。The following describes the embodiments in detail, but the embodiments are only used as examples, and are not intended to limit the scope of protection of the present invention. The following uses the same or similar symbols to indicate the same or similar elements for explanation.
請參照圖1至圖3,本發明第一實施例之凝聚粉體分散裝置主要包括噴嘴10、基座20、衝擊球30與夾持片40;其中噴嘴10內部具有一進氣道11,用以提供凝聚粉體AP混合適當氣體後噴入本發明裝置之內部;基座20內部亦具有一出氣道21且與進氣道11相對,噴嘴10與基座20相互對準後可以螺絲(未圖示)鎖固,並可形成一衝擊室IS以安置衝擊球30與夾持片40,衝擊室IS可以單獨地或共同地在噴嘴10或及基座20之內部形成,本發明並不加以限制。Please refer to FIG. 1 to FIG. 3. The condensed powder dispersing device according to the first embodiment of the present invention mainly includes a nozzle 10, a base 20, an impact ball 30, and a holding piece 40. The nozzle 10 has an air inlet 11 inside. In order to provide condensed powder AP and mix the appropriate gas, it is sprayed into the interior of the device of the present invention; the base 20 also has an air outlet 21 and is opposite to the air inlet 11, the nozzle 10 and the base 20 can be screwed (not (Illustrated) lock, and an impact chamber IS can be formed to house the impact ball 30 and the clamping piece 40. The impact chamber IS can be formed separately or collectively inside the nozzle 10 or the base 20, which is not included in the present invention. limit.
衝擊球30舉例為一球體,但除了平板外,本發明並不加以限制,任何具有凸出弧面之塊體均可適用。衝擊球30可藉由焊接、螺絲、夾持等方式安置在夾持片40之中央部位,圖1至圖2中之衝擊球30是以焊接方式固定於夾持片40上為例,夾持片40為一片體,中央部位之孔42可依與衝擊球30之安置方式決定是否製出,周圍部位則有多數通孔41,用以連通衝擊室IS與出氣道21,使經衝擊分散後之粉體P與氣流通過夾持片40到出氣道21。The impact ball 30 is exemplified as a sphere, but the invention is not limited except for a flat plate, and any block having a convex arc surface can be applied. The impact ball 30 can be placed at the center of the clamping piece 40 by welding, screws, clamping, etc. The impact ball 30 in FIGS. 1 and 2 is fixed to the clamping piece 40 by welding as an example. The sheet 40 is a piece of body. The hole 42 in the central part can be determined according to the arrangement of the impact ball 30. The surrounding part has a large number of through holes 41, which are used to connect the impact chamber IS and the air outlet 21 to disperse the impact. The powder P and the air flow pass through the holding piece 40 to the air outlet 21.
請參照圖4,依據粉體衝擊分離法理論,當欲分離不同粒徑之粉體時,其截斷粒徑(truncation particle size)與斯托克斯數(Stokes number, Stk)及W/S比值有關,由於本發明旨在分散凝聚之單一粒徑的粉體而非篩分不同粒徑的混合粉體,因此當欲分散之凝聚粉體的粒徑與密度確定後,便可依據其斯托克斯數選擇適當之尺寸參數與氣流流量或流速,其中W表示噴嘴寬度,S表示衝擊距離,D表示衝擊球直徑或寬度,本發明建議但不限制,其中斯托克斯數為2.0~66.2,W/S比值為0.1~5.0,W/D為0.1~1.0;經一實驗可知,本發明之分散裝置可有效分散粉體粒徑至少到2.29微米,所對應之斯托克斯數最低到2.0。Please refer to Figure 4. According to the theory of powder impact separation method, when the powders with different particle sizes are to be separated, the truncation particle size, Stokes number (Stk), and W / S ratio Relevantly, since the present invention aims to disperse agglomerated powders of a single particle size rather than sieving mixed powders of different particle sizes, when the particle size and density of the agglomerated powders to be dispersed are determined, it can be based on its particle size. Choose the appropriate size parameter and air flow or flow rate, where W is the nozzle width, S is the impact distance, and D is the diameter or width of the impact ball. The present invention suggests but is not limited, and the Stokes number is 2.0 ~ 66.2 , W / S ratio is 0.1 ~ 5.0, W / D is 0.1 ~ 1.0; after an experiment, it can be known that the dispersion device of the present invention can effectively disperse the powder particle size to at least 2.29 microns, and the corresponding Stokes number is as low as 2.0.
本發明第二實施例,如圖5所示,亦可以二片夾持片40配合適當尺寸之孔42,例如孔42之直徑不大於衝擊球30之直徑,以上下各一片夾持衝擊球30並固定於衝擊室IS中,如此使衝擊球30可隨氣流而轉動。In the second embodiment of the present invention, as shown in FIG. 5, two clamping pieces 40 may be matched with holes 42 of an appropriate size. For example, the diameter of the holes 42 is not larger than the diameter of the impact ball 30. It is fixed in the impact chamber IS, so that the impact ball 30 can rotate with the airflow.
本發明第三實施例,如圖6所示,亦可以在夾持片40上中央部位先固定一夾爪43,再用以夾持衝擊球30並固定於衝擊室IS中,此夾爪43可以由夾持片40衝壓而成或是另一片體,夾爪43具有多數單爪用以容納衝擊球30使可隨氣流而轉動。In the third embodiment of the present invention, as shown in FIG. 6, a clamping jaw 43 can also be fixed at the central part of the clamping piece 40 first, and then used to clamp the impact ball 30 and be fixed in the impact chamber IS. This clamping jaw 43 It can be punched from the clamping piece 40 or another piece. The clamping claw 43 has a plurality of single claws for receiving the impact ball 30 so as to be able to rotate with the airflow.
綜上所述,雖然本發明已以實施例揭露如上,然其並非用以限定本發明。本發明所屬技術領域中具有通常知識者,在不脫離本發明之精神和範圍內,當可作各種之更動與潤飾。因此,本發明之保護範圍當視後附之申請專利範圍所界定者為準。In summary, although the present invention has been disclosed as above with the embodiments, it is not intended to limit the present invention. Those with ordinary knowledge in the technical field to which the present invention pertains can make various changes and modifications without departing from the spirit and scope of the present invention. Therefore, the protection scope of the present invention shall be determined by the scope of the attached patent application.
10‧‧‧噴嘴10‧‧‧ Nozzle
IS‧‧‧衝擊室 IS‧‧‧Impact chamber
11‧‧‧進氣道 11‧‧‧air inlet
20‧‧‧基座 20‧‧‧ base
21‧‧‧出氣道 21‧‧‧Airway
30‧‧‧衝擊球 30‧‧‧ impact ball
40‧‧‧夾持片 40‧‧‧Clip
41‧‧‧通孔 41‧‧‧through hole
42‧‧‧孔 42‧‧‧hole
43‧‧‧夾爪 43‧‧‧Jaw
AP‧‧‧凝聚粉體 AP‧‧‧ agglomerated powder
P‧‧‧粉體 P‧‧‧ powder
圖1繪示本發明第一實施例之凝聚粉體分散裝置之分解圖。 圖2繪示本發明如圖1分散裝置之組合圖。 圖3繪示本發明如圖1分散裝置之夾持片之俯視圖。 圖4繪示本發明如圖1分散裝置之尺寸定義示意圖。 圖5繪示本發明第二實施例之組合示意圖。 圖6繪示本發明第三實施例之組合示意圖FIG. 1 illustrates an exploded view of a condensed powder dispersion device according to a first embodiment of the present invention. FIG. 2 illustrates a combination diagram of the dispersing device of FIG. 1 according to the present invention. FIG. 3 shows a top view of the holding sheet of the dispersing device of FIG. 1 according to the present invention. FIG. 4 is a schematic diagram illustrating the size definition of the dispersion device of FIG. 1 according to the present invention. FIG. 5 is a schematic diagram of the second embodiment of the present invention. FIG. 6 is a schematic diagram of a third embodiment of the present invention.
Claims (7)
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| Application Number | Priority Date | Filing Date | Title |
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| TW107134223A TWI677375B (en) | 2018-09-28 | 2018-09-28 | Agglomerated powder dispersion device |
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| TW107134223A TWI677375B (en) | 2018-09-28 | 2018-09-28 | Agglomerated powder dispersion device |
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| TWI677375B true TWI677375B (en) | 2019-11-21 |
| TW202012046A TW202012046A (en) | 2020-04-01 |
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| US20080029625A1 (en) * | 2005-07-07 | 2008-02-07 | Talton James D | Process for milling and preparing powders and compositions produced thereby |
| WO2013017463A1 (en) * | 2011-08-01 | 2013-02-07 | Wacker Chemie Ag | Process for producing dispersible powders |
| CN103043997A (en) * | 2011-10-11 | 2013-04-17 | 旭化成化学株式会社 | Powder, formed body, coated body and manufacturing method of powder |
| CN103977870A (en) * | 2014-05-26 | 2014-08-13 | 北京航空航天大学 | Process and device for preparing graphene precursor two-dimension nanoscale graphite powder by adopting airflow crushing and peeling method |
| TW201507784A (en) * | 2013-06-17 | 2015-03-01 | Ebara Corp | Powder discharge system |
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2018
- 2018-09-28 TW TW107134223A patent/TWI677375B/en active
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| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| US20040061007A1 (en) * | 2002-09-27 | 2004-04-01 | Milojevic Dragoslav K. | Swirl gun for powder particles |
| US20080029625A1 (en) * | 2005-07-07 | 2008-02-07 | Talton James D | Process for milling and preparing powders and compositions produced thereby |
| WO2013017463A1 (en) * | 2011-08-01 | 2013-02-07 | Wacker Chemie Ag | Process for producing dispersible powders |
| CN103043997A (en) * | 2011-10-11 | 2013-04-17 | 旭化成化学株式会社 | Powder, formed body, coated body and manufacturing method of powder |
| CN103043997B (en) | 2011-10-11 | 2016-01-20 | 旭化成化学株式会社 | The manufacture method of powder, molding, cladding and powder |
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| TW202012046A (en) | 2020-04-01 |
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