TW200948469A - Stirring device, stirrer, and stirring method - Google Patents
Stirring device, stirrer, and stirring method Download PDFInfo
- Publication number
- TW200948469A TW200948469A TW098101422A TW98101422A TW200948469A TW 200948469 A TW200948469 A TW 200948469A TW 098101422 A TW098101422 A TW 098101422A TW 98101422 A TW98101422 A TW 98101422A TW 200948469 A TW200948469 A TW 200948469A
- Authority
- TW
- Taiwan
- Prior art keywords
- container
- groove
- stirring
- agitating
- stirrer
- Prior art date
Links
Classifications
-
- B—PERFORMING OPERATIONS; TRANSPORTING
- B02—CRUSHING, PULVERISING, OR DISINTEGRATING; PREPARATORY TREATMENT OF GRAIN FOR MILLING
- B02C—CRUSHING, PULVERISING, OR DISINTEGRATING IN GENERAL; MILLING GRAIN
- B02C17/00—Disintegrating by tumbling mills, i.e. mills having a container charged with the material to be disintegrated with or without special disintegrating members such as pebbles or balls
- B02C17/04—Disintegrating by tumbling mills, i.e. mills having a container charged with the material to be disintegrated with or without special disintegrating members such as pebbles or balls with unperforated container
- B02C17/08—Disintegrating by tumbling mills, i.e. mills having a container charged with the material to be disintegrated with or without special disintegrating members such as pebbles or balls with unperforated container with containers performing a planetary movement
-
- 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
- B01F29/10—Mixers with rotating receptacles with receptacles rotated about two different axes, e.g. receptacles having planetary motion
-
- 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
- B01F29/90—Mixers with rotating receptacles with stirrers having planetary motion
-
- B—PERFORMING OPERATIONS; TRANSPORTING
- B02—CRUSHING, PULVERISING, OR DISINTEGRATING; PREPARATORY TREATMENT OF GRAIN FOR MILLING
- B02C—CRUSHING, PULVERISING, OR DISINTEGRATING IN GENERAL; MILLING GRAIN
- B02C17/00—Disintegrating by tumbling mills, i.e. mills having a container charged with the material to be disintegrated with or without special disintegrating members such as pebbles or balls
- B02C17/10—Disintegrating by tumbling mills, i.e. mills having a container charged with the material to be disintegrated with or without special disintegrating members such as pebbles or balls with one or a few disintegrating members arranged in the container
Abstract
Description
200948469 六、發明說明: 【發明所屬之技術領域】 本發明係關於一種攪拌裝置、攪拌子及攪拌方法。本發 明係特別關於-種具有BJ形的外周面,將包含於擾掉物中 的凝集物效率佳地磨潰的攪拌裝置'攪拌子及攪拌方法。 又,本申請案係與下述曰本申請案相關,+ 彔相關主張來自下述的 曰本申請案的優先權的申請案1 申請曰2008年1 ❿ 1·日本專利申請案特願2008-Ή51 月16曰 【先前技術】 先前,已知有攪拌液體時所用的攪拌子。例如,專 獻1中揭示-種攪拌子’其為魚板形狀,且其底面中 隆起。專利…中所記載的授拌子,係於授拌子的;200948469 VI. Description of the Invention: TECHNICAL FIELD OF THE INVENTION The present invention relates to a stirring device, a stirring device and a stirring method. The present invention relates to a stirring device "agitating means and a stirring method" which have a BJ-shaped outer peripheral surface and which efficiently agglomerate the aggregate contained in the scrambled material. Further, the present application is related to the following application, and the related claims are from the following priority application of the present application. 1 Application 曰 2008 1 ❿ 1 Japanese Patent Application 2008- Ή51月16曰[Prior Art] Previously, a stirrer used when stirring a liquid was known. For example, the stirrer disclosed in the '1' is in the shape of a fish plate and has a bulge in the bottom surface thereof. The stir-mixer described in the patent is attached to the stirrer;
埋設鐵芯,而將其製作成不會傾倒。在專利文獻2中 揭示一種使授拌容器'邊自轉,—邊繞著公轉㈣公轉= 行星式攪拌裝置。 [專利文獻1] [專利文獻2] 曰本專利公開公報特 曰本專利公開公報特 開平4— 57238號 開 2000 — 84388 號 【發明内容】 [發明所欲解決之問題] 專利文獻1中所記載的攪拌子, 因其底面中央部隆起, 200948469 當使用於專利文獻2中所記載的行星式攪拌裝置中時,容 易於上下方向彈跳。再者,因具有突起或角,而無法於攪 拌容器内滑順地接觸滑動。其結果,專利文獻丨中記裁的 攪拌子,無法使用於使液體中初級粒子凝集的凝集物分散 ‘ 的用途。特別是,初級粒子為數微米至次微米的粒子的情 況時無法細敏地分散。 對此,本發明的其中一層面中,以提供可解決上述的 肖題的授拌裝置、擾拌子及授拌方法為其目的。此目的係 罾藉由申請專利範圍中的獨立項中記載的特徵的組合而達 成。又’附屬項係規定本發明的更有利的具體例。 [解決問題之技術手段] 為了解決上述課題,本發明的第一形態中,提供一種 • 攪拌裝置,其係具備·· 攪拌物要被置入之攪拌容器; 使上述攪拌容器旋轉之旋轉部;以及 ❹ 、攪伴子’其外周面為圓形,與上述攪拌物一起被置入 撥拌各器中’並具有用以磨潰上述授拌物中所包含的 凝集物之磨潰部、及將上述授拌物引入上述磨潰部之弓卜 本發明的第二形態中’提供-種攪拌子,其係異備: ^ 包含的凝集物,在與攪拌容器的内面之間磨 :::::周:—上述磨溃部之引一 本發月的第三形態中,提供一種攪拌方法,其係異備: 4 200948469 準備攪拌子的步驟,該 撸棘早甘& 丁疋外形為大約圓柱形的 及傾L 有相對於授拌容器内底面之相對面、側面 =1;該傾斜部與上述内底面呈銳角,且連接上述相 對面與上述側面; τ 、將授拌物與上述授拌子置入上述擾摔容器中的步驟; 以及 藉由旋轉部,使上述攪拌容器旋轉的步驟;The core is buried and made so that it does not fall. Patent Document 2 discloses a method in which the mixing container is rotated while rotating around (four) revolution = planetary stirring device. [Patent Document 1] [Patent Document 2] Japanese Laid-Open Patent Publication No. Hei-4-57238-A No. 2000-84388 [Draft of the Invention] [Problems to be Solved by the Invention] Patent Document 1 When the stirrer is raised at the center of the bottom surface, 200948469 is easy to bounce in the vertical direction when used in the planetary stirring device described in Patent Document 2. Further, since it has projections or corners, it is impossible to smoothly contact the sliding in the agitating container. As a result, the stirrer described in the patent document can not be used for the purpose of dispersing agglomerates in which primary particles are aggregated in a liquid. In particular, when the primary particles are particles of several micrometers to submicrometers, they cannot be finely dispersed. In this regard, in one aspect of the present invention, it is an object to provide a mixing device, a scrambler, and a mixing method that can solve the above-mentioned problems. This object is achieved by a combination of features recited in separate items in the scope of the patent application. Further, the subsidiary item defines a more advantageous specific example of the present invention. [Means for Solving the Problems] In order to solve the above problems, a first aspect of the present invention provides a stirring device including: a stirring container into which a stirring material is placed; and a rotating portion that rotates the stirring container; And the enthalpy and the companion "the outer peripheral surface is circular, and is placed in the mixing device together with the agitating material" and has a pulverizing portion for abrading the agglomerates contained in the above-mentioned admixture, and The above-mentioned nutrient is introduced into the above-mentioned pulverizing portion. In the second aspect of the present invention, a kind of stirrer is provided, which is heterogeneous: ^ The contained agglomerate is ground between the inner surface of the stirring vessel:::: : Week: - In the third form of the above-mentioned pulverizing section, a stirring method is provided, which is different: 4 200948469 The step of preparing the stirring, the shape of the thorns and the tings are approximately The cylindrical shape and the tilting L have opposite sides with respect to the inner bottom surface of the mixing container, and the side surface=1; the inclined portion has an acute angle with the inner bottom surface, and connects the opposite surface to the side surface; τ, the composition and the above-mentioned teaching Steps in which the stirrer is placed in the above-mentioned disturbing container And a step of rotating the agitating vessel by a rotating portion;
在使上述攪拌容器旋轉的步驟中,將上述攪拌物引入 上述内底面與上述傾斜部之間,並藉由上述内底面與上述 相對面之間的接觸滑動’磨潰上述攪拌物中所包含的凝集 體。 ’、 又,上述的發明的概要,並非列舉全部的本發明的必 •要的特徵,這些特徵群的副組合亦另可成為發明。 [功效] 若根據本發明,即可提供一種適於使液體中初級粒子 〇 凝集的凝集物分散的用途的攪拌裝置、攪拌子及攪拌方 法。特別是’可提供一種初級粒子為數微米至次微米的粒 子的情況時’可使其細緻地分散的攪拌裝置、攪拌子及挽 拌方法。 【實施方式】 以下,通過發明的實施形態來說明本發明的其中一個 層面,但以下的實施形態並非用以限定申請專利範圍所請 200948469 之發明;X ’實施形態之中所說明的特徵的組合的全部, 並不-定是發明的解決手段所必須。又,以下,參照圖°式: 說明實施形態,但圖式的記載中,有於相同或類似的二 標示相同符號,而省略重複說明的情況。另外,圖式係77 式地表示者,其厚度與平面尺寸之間的關係、比率等:: 與實際者相異的情況。為了說明的方便,目式相互間亦有 包含相互的尺寸的關係或比率相異的部分的情況。 鲁 m 第1圖係表示以垂直於水平方向的平面來切斷本實施 形態的攪拌裝置10而得的剖面圖。攪拌裝置1〇,具備攪 拌容器100、旋轉部104及攪拌子108,將已置入其内部的 攪拌物20中所包含的凝集物24磨潰。攪拌容器1〇〇,可 為有底的圓筒形狀,攪拌容器1〇〇具有蓋部11〇、周壁部 112、底板部114及腳輪(caster)U6。蓋部11〇被配置於攪 拌容器1〇〇的上部,可為圓板形狀。周壁部112可為圓筒 形狀,包含面向攪拌容器100的外側之外壁面122及面向 攪拌容器1〇〇的内側之内壁自124。底板部114被配置於 攪拌容器100的底部,可為圓板形狀,底板部114包含面 向授拌容肖1GG的外側之外底面132、以及面向擾摔容器 100的内侧之内底面134。内底面134與内壁面124 一起形 成内面118。腳輪116,例如可採用滾珠腳輪(baiicaster), 被配置於底板部114的外底面132,以降低攪拌容器1〇〇 的滑動摩擦。 蓋部11〇、周壁部112、底板部114,可為聚丙烯、氟 化樹脂、橡膠等的樹脂,亦可為不油(sus)等的金屬。 6 200948469 底板》P 114可與周壁部112 —體地形成,底板部114亦可 與周壁部112滑順地結合。攪拌容器100亦可為聚丙烯製 而其内輕為56mm的圓筒形狀。又,在實施形態中,有將 置蓋邻Π 〇的一側記載為上側,而將配置底板部1丨4的 一側記載為下側的情況。然而,如此的記載並非用以將攪 摔容器100的使用限定於圖示的方向。In the step of rotating the agitating vessel, the agitating material is introduced between the inner bottom surface and the inclined portion, and is slid by contact between the inner bottom surface and the opposite surface to abrade the inclusion of the agitating substance. Condensed. Further, the summary of the above invention does not recite all of the essential features of the present invention, and the sub-combination of these feature groups may also be an invention. [Effect] According to the present invention, it is possible to provide a stirring device, a stirring bar and a stirring method for use in which agglomerates for agglomerating primary particles in a liquid are dispersed. In particular, when a kind of particles having a primary particle of several micrometers to a micrometer can be provided, a stirring device, a stirring bar and a stirring method which can be finely dispersed can be provided. [Embodiment] Hereinafter, one embodiment of the present invention will be described by way of embodiments of the invention. However, the following embodiments are not intended to limit the invention of the patent application No. 200948469; the combination of features described in the X' embodiment All of them are not necessarily required for the solution of the invention. In the following description, the same or similar reference numerals will be given to the same or similar reference numerals, and the description thereof will not be repeated. In addition, the drawings are expressed in the form of 77, the relationship between the thickness and the plane size, the ratio, and the like:: A case different from the actual one. For the convenience of explanation, there are cases where the meshes have mutually different dimensional relationships or ratios. Lu m Fig. 1 is a cross-sectional view showing the stirring device 10 of the present embodiment cut in a plane perpendicular to the horizontal direction. The stirring device 1A includes a stirring container 100, a rotating portion 104, and a stirring member 108, and the aggregate 24 contained in the agitated material 20 placed therein is pulverized. The agitating vessel 1 is formed into a bottomed cylindrical shape, and the agitating vessel 1 has a lid portion 11A, a peripheral wall portion 112, a bottom plate portion 114, and a caster U6. The lid portion 11A is disposed on the upper portion of the agitating vessel 1A and may have a circular plate shape. The peripheral wall portion 112 may have a cylindrical shape including an outer wall surface 122 facing the outer side of the agitating vessel 100 and an inner wall 124 facing the inner side of the agitating vessel 1 . The bottom plate portion 114 is disposed at the bottom of the agitating vessel 100 and may have a circular plate shape. The bottom plate portion 114 includes an outer bottom surface 132 facing the mixing chamber 1GG and an inner bottom surface 134 facing the inner side of the scramble container 100. The inner bottom surface 134 forms an inner surface 118 with the inner wall surface 124. The caster 116 can be disposed, for example, by a ball caster (baiicaster) on the outer bottom surface 132 of the bottom plate portion 114 to reduce the sliding friction of the agitating container 1〇〇. The lid portion 11A, the peripheral wall portion 112, and the bottom plate portion 114 may be a resin such as polypropylene, fluororesin, or rubber, or may be a metal such as sus. 6 200948469 The bottom plate 》P 114 may be integrally formed with the peripheral wall portion 112, and the bottom plate portion 114 may also be smoothly coupled with the peripheral wall portion 112. The agitating vessel 100 may also be made of polypropylene and having a cylindrical shape with a light inside of 56 mm. Further, in the embodiment, the side on which the adjacent Π is placed is referred to as the upper side, and the side on which the bottom plate portion 丨4 is disposed is referred to as the lower side. However, such a description is not intended to limit the use of the disrupting container 100 to the illustrated orientation.
% 旋轉部104’可為所謂的行星式旋轉裝置,使攪拌容器 100旋轉。旋轉部104,可使攪拌容器1〇〇 一邊繞著垂直於 水平的公轉轴A1作公轉,一邊亦可使攪拌容器1〇〇作自 轉。旋轉部104,具有公轉容器140、曲柄15〇、轴承152 及轴桿154。旋轉部104,具有馬達156、平衡配重158、 ^寺部160及腳部162。公轉容胃14〇,可為其内徑較授摔 容器1〇〇的外徑大的有底的圓筒形狀,於公轉容器i4〇的 内部則配置有攪拌容器1 〇〇。 公轉容器140,包含筒壁部142、筒底部144及轴j 146。筒壁部142 ’可為沿著公轉容器14〇的自轉軸… 伸的圓筒形狀《筒底部144,可與筒壁部142的一端結合 被配置於公轉容器140的底部,而為圓板形狀亦可二 壁部I42 一體地形成。筒壁部142、筒底部144,可為聚? 稀、氟化樹脂、橡膠等的樹脂,亦可為不鏽鋼等的金屬 軸部被配置於筒底部144的外側,從筒底部144白The % rotating portion 104' may be a so-called planetary rotating device that rotates the agitating vessel 100. The rotating portion 104 allows the stirring container 1 to rotate while rotating around the horizontal axis A1 perpendicular to the horizontal axis. The rotating portion 104 has a revolution container 140, a crank 15A, a bearing 152, and a shaft 154. The rotating portion 104 has a motor 156, a balance weight 158, a temple portion 160, and a leg portion 162. The crutches of the stomach are 14 inches, and the inner diameter thereof is larger than the outer diameter of the outer diameter of the container, and the inside of the revolution container i4 is disposed with the stirring container 1 . The revolution container 140 includes a cylinder wall portion 142, a cylinder bottom portion 144, and a shaft j 146. The cylindrical wall portion 142' may be a cylindrical shape "the barrel bottom portion 144 extending along the rotation axis of the revolution container 14", and may be disposed at the bottom of the revolution container 140 in combination with one end of the cylindrical wall portion 142, and has a circular plate shape. The two wall portions I42 may also be integrally formed. The wall portion 142 and the bottom portion 144 of the tube can be gathered? A resin such as a dilute, a fluorinated resin or a rubber may be arranged such that a metal shaft portion such as stainless steel is disposed outside the cylinder bottom portion 144, and is white from the cylinder bottom portion 144.
中心向旋轉部HM的外倒,沿著公轉容器㈣的自轉轴A 延伸》公轉容器亦可為氟化樹脂製而其内徑為ι〇 筒形狀。 200948469 公轉3 為向水平方向延伸的角柱形狀,用以支持 轉合器140。軸承152,被配置於曲柄 公轉容器糊的㈣146插诵㈣ 〇的-端’因被 支mi 轴承152係將公轉容器140 ::成可作旋轉。馬達156’係經由抽桿154而與曲柄15〇 ::公轉轴A1作為中心’而使曲柄15。旋轉…柄 1另一端’亦可配置平衡配重158。支持部16〇可為用 支持馬冑156之框體’腳部162可從下方來支持支持部The center is turned outwardly from the rotating portion HM, and extends along the rotation axis A of the revolution container (four). The revolution container may be made of a fluorinated resin and have an inner diameter of an iv tube shape. 200948469 The revolution 3 is a column shape extending in the horizontal direction to support the adapter 140. The bearing 152 is disposed in the crank of the crank revolving container paste (four) 146, and the end of the crucible (four) is rotated by the revolving container 140: The motor 156' causes the crank 15 via the drawbar 154 with the crank 15 〇 :: the revolving axis A1 as the center '. The balance weight 158 can also be configured by rotating the handle 1 at the other end. The support portion 16 can be used to support the frame 162 of the stable 156. The foot portion 162 can support the support portion from below.
〇。另外’公轉容器刚與支持部160’例如隔著彈性構 牛而結合,可抑制公轉容器140的自轉。 接著,使用第1圖來說明旋轉部104 藉由馬…,公轉容器14。可一邊抑制自=公 轉軸Ai為中心作公轉。若公轉容器14〇公轉,則被配置於 内部的攪拌容器100,伴隨著公轉容器14〇而以公轉轴A1 為中心作公轉。開始公轉後的攪拌容器100,藉由離心力 的作用,於筒底部144的内面上滑動,並推壓筒壁部142 的内面。攪拌容器1〇〇,藉由外壁面122與筒壁部142之 間作用的摩擦力等,於筒壁部142的内面上轉動,並以自 轉軸A3為中心作自轉。在此,公轉容器14〇的自轉軸 亦可具有傾斜角S1而朝向公轉軸A1側傾斜。藉此,公轉 容器140,於公轉中,持續向公轉轴A1側傾斜。因此,作 用於授拌容器100上的離心力,係具有:將攪拌容器1〇〇 向筒壁部142推壓的力、以及將攪拌容器100向筒底部144 推壓的力之二成分。 攪拌子108,係與攪拌物2〇 一起被置入攪拌容器ι〇〇 8 200948469 參 的内4。撥拌子l〇8的外徑,可小於内壁面i24的半徑。 :轉谷器140公轉時’授拌子⑽伴隨著公轉容器14〇而 以公轉轴A1為中心作公轉。開始公轉後的攪拌子⑽藉 由離心力F1 $作用,向攪拌容器1〇〇的内壁面124被推 壓。攪拌+ 108 ’藉由與外壁自122之間作用的摩擦力等, 於内壁面124上轉動,並以自轉袖A4為中心作自轉。在此, 公轉容器140的自轉軸A2向公轉軸ah則傾斜時作用於 攪拌子108上的離心力F卜係具有將攪拌子ι〇8向内壁面 124推壓的「推壓力F2」、以及將攪拌子1〇8向内底面Η* 推壓的「推壓力F3」之二成分β藉此,公轉容器14〇,係 藉由攪拌容器1〇〇的旋轉,對攪拌子1〇8賦予:攪拌子1〇8 向攪拌容器100的内壁面124被推壓的推壓力1?2的作用、 以及攪拌子108向攪拌容器100的内底面134被推壓的推 壓力F3的作用。 第2圖係表示攪拌容器100、攪拌子1〇8及公轉容器 140的旋轉運動的概要。公轉容器14〇 一邊抑制自轉,一 邊例如順時鐘旋轉地繞著公轉轴A1作公轉。授拌容器 100,與公轉容器140 —起順時鐘旋轉地繞著公轉軸A1作 公轉。因公轉容器140的自轉受到抑制,授拌容器丨〇〇, 向公轉容器14〇的公轉方向的相反方向,亦即,逆時鐘旋 轉地作自轉。攪拌子’係與攪拌容器1〇〇 一起順時鐘 旋轉地繞著公轉軸A1作公轉,藉由攪拌容器1〇〇的自轉, 向與攪拌容器100的自轉相同方向,亦即逆時鐘旋轉地作 自轉。另外,雖然以公轉容器140繞著公轉軸A1向順時鐘 200948469 方向作旋轉的情況來說明,但公轉容器14〇的旋轉方向不 限於此。 又’在第1圖與第2圖中’係說明了利用公轉容器14〇 一邊抑制自轉一邊以公轉轴A1為中心作公轉,使攪拌容器 100於公轉容器140的筒壁部142的内面上轉動(滾動),並 以自轉軸A3為中心作自轉的情況,但旋轉部1〇4使攪拌容 器旋轉的方法不限於此。作為其他方法,例如,亦可 ❿ 將攪拌容器100固定於公轉容器140的内部,利用使公轉 容器14〇 一邊以自轉轴A2為中心作旋轉,一邊以公轉軸 A1為中心作公轉,使攪拌容器1〇〇 一邊自轉,一邊以公轉 轴A1為中心作公轉,此時,攪拌容器1〇〇,亦可被固定於 公轉容器140,使自轉軸A3與公轉容器14〇自轉軸A2大 約位於同直線上。又,授拌容器的外徑與公轉容器 140的内徑大約相同,則攪拌容器1〇〇的外壁面122也可 連接公轉容器140的筒壁部142而被固定。 _ 帛3 ®係表示本實施形態的授拌子1〇8的側面圖的一 例。第4圖係表示本實施形態的擴摔子1〇8的底面圖的一 例。以下’使用第3圖與第4圖來說明攪拌子⑽。如第3 圈所示,挽拌子⑽可具有以自轉轴A4作為對稱軸的旋轉 體形狀。藉此,可使擾拌子1〇8的磨耗降低。㈣子1〇8 亦可由垂直於自轉轴A4,並包含擾掉子1〇8的中心的平面 P作為對稱面,而被形成面對稱。藉此,授拌子⑽的外 形係被形成上下對稱。 10 200948469 首先,說明攪拌子108的機能。攪拌子108,具有磨潰 部2〇0及引入部202。磨潰部2〇〇具有將攪拌物20中所包 含的凝集# 24磨潰的機能。磨潰部2〇〇,係將攪拌物 中所包含的凝集物24,於與攪拌容器1〇〇的内面ιΐ8之間 磨凊攪拌物20中所包含的初級粒子(口他町卿价16)22, 凝集而形成凝集物24。㈣子⑽以適度的力量磨潰凝集 物24,藉此可瓦解凝集物24,而分散成為初級粒子^為 止0 引入部202’具有將攪拌物2〇引入磨潰部2〇〇的機能。 引入邛202,亦可連接配置於磨潰部2〇〇。藉此因凝集物 Μ有效率地供給至磨潰部2⑼,心效率佳地使初級粒子 22分散。另外,磨潰部2〇〇與引入部2〇2的機能,係於攪 ^子108的複數之處發揮作用。再者,兩機能並非可明確 區別者’構成磨潰部200的構件,亦可具有引入部2〇2的 機龅’構成引入部202的構件,亦可具有磨潰部2〇〇的機 能。 接著,參照第3圖來說明攪拌子1〇8的構成的一例。 攪拌子108,具有外周面21〇、相對面24〇及頂面25〇。外 周面210’係向攪拌子108的自轉軸A4方向延伸而形成 可連接相對面240與頂面250。外周面21〇可具有圓形的 卜形,例如,可具有向自轉轴A4方向延伸的大約圓柱形的 ^藉此,挽拌子108係具有向自轉轴A4方向延伸的圓 周面,因而與攪拌容器100的内壁面124抵接的面積變大, 可減少攪拌子108以及内壁面124的磨耗、攪拌子ι〇8可 200948469 於攪拌容器100的内部安定地旋轉。外周面210亦可配合 攪拌容器100的内壁面124的形狀而形成,上述大約圓柱 形的外形的自轉轴A4方向的至少一端,亦可越向端部,其 外徑變成越小。Hey. Further, the "revolving container" is coupled to the support portion 160', for example, via an elastic cow, and the rotation of the revolution container 140 can be suppressed. Next, using the first drawing, the rotating unit 104 will be described as a revolving container 14 by a horse. It is possible to suppress the rotation from the A-axis Ai as a center. When the revolution container 14 is revolved, the agitating container 100 disposed inside is revolved around the revolution axis A1 with the revolution container 14A. The agitating vessel 100 that has started to revolve is slid on the inner surface of the cylinder bottom portion 144 by the action of centrifugal force, and presses the inner surface of the cylinder wall portion 142. The agitating vessel 1 is rotated by the frictional force acting between the outer wall surface 122 and the tubular wall portion 142 on the inner surface of the tubular wall portion 142, and is rotated about the rotation axis A3. Here, the rotation axis of the revolution container 14A may also have an inclination angle S1 and be inclined toward the revolution axis A1 side. Thereby, the revolution container 140 is continuously inclined toward the revolution axis A1 side during the revolution. Therefore, the centrifugal force applied to the mixing container 100 has two components: a force for pressing the agitating vessel 1 to the tubular wall portion 142 and a force for pressing the agitating vessel 100 toward the tubular bottom portion 144. The stirrer 108 is placed in the mixing vessel 〇〇 8 200948469 with the agitator 2〇. The outer diameter of the dialing pin l8 can be smaller than the radius of the inner wall surface i24. When the rotary turret is at 140 rpm, the tweezer (10) revolves around the revolution axis A1 with the revolution container 14 。. The stirrer (10) after the start of the revolution is pushed by the centrifugal force F1$ to the inner wall surface 124 of the agitating vessel 1〇〇. The stirring + 108 ' is rotated on the inner wall surface 124 by the frictional force acting on the outer wall from 122, and is rotated about the rotation sleeve A4. Here, the centrifugal force F acting on the agitating member 108 when the rotation axis A2 of the revolution container 140 is inclined toward the revolution axis ah has a "pushing pressure F2" for pressing the agitating bar ι 8 against the inner wall surface 124, and The two components β of the "pushing pressure F3" which are pushed by the stirring member 1〇8 to the inner bottom surface Η* are rotated by the stirring container 1〇〇, and the stirring member 1〇8 is given: stirring. The action of the pressing force 1?2 which is pressed against the inner wall surface 124 of the stirring container 100 and the pressing force F3 which the stirring element 108 is pressed against the inner bottom surface 134 of the stirring container 100 acts. Fig. 2 is a view showing the outline of the rotational movement of the agitating vessel 100, the agitator 1〇8, and the revolution container 140. The revolution container 14 公 revolves around the revolution axis A1 while rotating, for example, clockwise. The mixing container 100 revolves around the revolution axis A1 in clockwise rotation with the revolution container 140. Since the rotation of the revolving container 140 is suppressed, the mixing container 丨〇〇 is rotated in the opposite direction to the revolution direction of the revolving container 14 ,, that is, counterclockwise. The stirrer 'revolves around the revolution axis A1 clockwise with the stirring vessel 1 ,, and rotates in the same direction as the rotation of the stirring vessel 100 by the rotation of the stirring vessel 1 , that is, counterclockwise rotation. Further, the case where the revolution container 140 rotates in the direction of the clockwise 200948469 around the revolution axis A1 is described, but the rotation direction of the revolution container 14A is not limited thereto. In the first and second drawings, the revolving container 100 is rotated around the revolving axis A1 while suppressing the rotation, and the agitating container 100 is placed on the inner surface of the cylindrical wall portion 142 of the revolving container 140. The rotation (rolling) is performed with the rotation axis A3 as the center, but the method of rotating the stirring container by the rotating portion 1〇4 is not limited thereto. As another method, for example, the stirring container 100 may be fixed to the inside of the revolving container 140, and the revolving container 14 may be rotated around the rotation axis A2 while being rotated around the revolving axis A1 to stir. The container 1 revolves while revolving around the revolving axis A1. At this time, the agitating container 1〇〇 can be fixed to the revolving container 140 so that the rotation axis A3 and the revolving container 14 are located approximately from the rotation axis A2. On the same line. Further, the outer diameter of the mixing container is approximately the same as the inner diameter of the revolution container 140, and the outer wall surface 122 of the stirring container 1 can be connected to the cylindrical wall portion 142 of the revolution container 140 to be fixed. _ 帛 3 ® is an example of a side view of the stirrer 1 8 of the present embodiment. Fig. 4 is a view showing an example of a bottom view of the spreader 1〇8 of the present embodiment. The stirrer (10) will be described below using Figs. 3 and 4. As shown in the third lap, the plucking body (10) may have a shape of a rotator having the rotation axis A4 as an axis of symmetry. Thereby, the abrasion of the scrambler 1〇8 can be reduced. (4) The sub-portion 8 8 may be formed to be plane-symmetric by a plane P perpendicular to the rotation axis A4 and including the center of the disturbing sub-frame 1 8 as a plane of symmetry. Thereby, the outer shape of the stir frit (10) is formed to be vertically symmetrical. 10 200948469 First, the function of the stirrer 108 will be described. The agitator 108 has a pulverizing portion 2〇0 and a lead-in portion 202. The pulverizing portion 2 has a function of pulverizing the agglomerate #24 contained in the agitating material 20. In the pulverizing portion 2, the primary particles contained in the agitating material 20 are honed between the aggregate 24 contained in the agitating material and the inner surface ι 8 of the agitating vessel 1 (Kurota-cho, price 16) 22, agglutination to form agglomerates 24. (4) The sub-(10) abrades the aggregate 24 with a moderate force, whereby the aggregate 24 is disintegrated and dispersed into the primary particles. The introduction portion 202' has a function of introducing the agitated material 2〇 into the pulverizing portion 2〇〇. The crucible 202 is introduced, and may be connected to the pulverizing portion 2〇〇. Thereby, the aggregates are efficiently supplied to the pulverizing portion 2 (9), and the primary particles 22 are dispersed efficiently. Further, the function of the pulverizing portion 2A and the introducing portion 2〇2 functions in the plural of the agitating member 108. Further, the two functions are not clearly distinguishable from the members constituting the pulverizing portion 200, and the shackles of the introducing portion 2'2 constitute the members of the introducing portion 202, and may have the function of the pulverizing portion 2''. Next, an example of the configuration of the stirring unit 1〇8 will be described with reference to Fig. 3 . The agitator 108 has an outer peripheral surface 21A, an opposite surface 24A, and a top surface 25A. The outer peripheral surface 210' extends in the direction of the rotation axis A4 of the agitating member 108 to form the connectable opposing surface 240 and the top surface 250. The outer peripheral surface 21A may have a circular shape, for example, may have an approximately cylindrical shape extending in the direction of the rotation axis A4, and the plucking 108 has a circumferential surface extending in the direction of the rotation axis A4, thus stirring The area in which the inner wall surface 124 of the container 100 abuts increases, and the agitation of the agitator 108 and the inner wall surface 124 can be reduced, and the agitator ι 8 can be stably rotated inside the agitation vessel 100 at 200948469. The outer peripheral surface 210 may be formed in a shape matching the inner wall surface 124 of the agitating vessel 100, and at least one end of the approximately cylindrical outer shape in the direction of the rotation axis A4 may be smaller toward the end portion.
外周面210 ’包含側面212及外周傾斜部214。侧面 212,可被配置於攪拌子1〇8的自轉轴人4方向的中央附近。 侧面212可具有大約圓柱形狀的外形。側面212可形成與 攪拌容器100的内壁面124相對。側面212可為磨潰部 的一例。外周傾斜部214,係被配置成可連接側面212與 相對面240或頂面25〇β外周傾斜部214,可從側面^^起 越向相對面240或頂面25〇,其直徑變成越小。外周傾斜 部214 ’可為引入部2〇2的一例。 外周傾斜部214 ’可具有錐形部222、弧狀部 形部226及弧狀部228。錐形部222與弧狀部…,可被配 置於側面212起的向職25() ,錐形部咖與孤狀部 228 ’可被配置於側面212起的向相對面24〇側。錐形部 與錐形部226,係直線地連搂側自212與相對面或 頂面錐形部222與錐形部226,係具有切除圓錐形的 一部分後的外形。弧狀部224與弧狀部⑵係滑順地連接 侧面212與相對面24〇或頂面25〇。 錐形部222可與頂面250呈銳角S2,錐形部226可虚 相對面240呈銳角S2。藉此’包含相對面240的面盘外周 面㈣的距離,係隨著沿錐形部咖從側面2相 -漸漸地變窄。錐形部222、雜形部226、弧狀部: 12 200948469 ’錐形部226 與相對面240 弧狀部228,可為引入部202的一例,例如 可非為平面,而為弧狀部228或將側面212 滑順地連接的曲面。The outer peripheral surface 210' includes a side surface 212 and an outer peripheral inclined portion 214. The side surface 212 can be disposed in the vicinity of the center of the rotation axis of the agitator 1〇8 in the direction of the rotation axis. Side 212 can have a generally cylindrical shape. The side surface 212 may be formed opposite the inner wall surface 124 of the agitating vessel 100. The side surface 212 may be an example of a rupture portion. The outer peripheral inclined portion 214 is configured to connect the side surface 212 and the opposite surface 240 or the top surface 25〇β outer circumferential inclined portion 214, and the smaller the diameter becomes smaller from the side surface toward the opposite surface 240 or the top surface 25 . The outer peripheral inclined portion 214' may be an example of the introduction portion 2'2. The outer peripheral inclined portion 214' may have a tapered portion 222, an arcuate portion 226, and an arc portion 228. The tapered portion 222 and the arcuate portion ... can be disposed on the side surface 212 of the advancing 25 (), and the tapered portion and the odd portion 228 ' can be disposed on the side of the opposite side 24 from the side surface 212. The tapered portion and the tapered portion 226 are linearly connected to the side surface 212 and the opposite surface or the top surface tapered portion 222 and the tapered portion 226, and have a shape in which a part of the conical shape is cut away. The arcuate portion 224 and the arcuate portion (2) are smoothly connected to the side surface 212 and the opposite surface 24 or the top surface 25A. The tapered portion 222 may be at an acute angle S2 to the top surface 250, and the tapered portion 226 may be at an acute angle S2 to the imaginary opposing surface 240. Thereby, the distance from the outer peripheral surface (4) of the face plate including the opposite face 240 gradually decreases from the side surface 2 along the tapered portion. The tapered portion 222, the polygonal portion 226, and the curved portion: 12 200948469 'The tapered portion 226 and the opposite surface 240 the arc portion 228 may be an example of the introduction portion 202, and may be, for example, not a flat surface but an arc portion 228 Or a surface that smoothly connects the sides 212.
相對面240,當攪拌子1〇8被置入攪拌容器1〇〇時被 配置成相對於授拌容器⑽的内底面134。如第斗圖所示, 相對面240可為平坦面。相對面24()可為磨潰部勘的一 例。頂面250,係被配置於攪拌? 1〇8的相對面24〇的相 對的位置°頂面25G也可被配置成與相對面24G大約平行。 第5圓係表示另外的實施形態的攪拌子5G8。第5圖係 表示將挽拌子508於㈣子的中心附近向自轉轴A4 方向切斷時的剖面圖°第5圖係表示將挽拌物2G與擾拌子 5〇8置入授拌容器_ 然後藉由旋轉部⑽使授摔容 器100旋轉的狀態的概要。 首先說明授拌子508的構成的一例。授捧子5〇8具 有外周面510、底部Μη 3® TS工, 低"Ί 530及頂面25〇。外周面51〇,係對應 外周面2Η) ’向攪拌子5〇8的自轉軸Α4方向延伸並形成 可連接頂面250與相對面54〇。外周面51〇,包含側面^】、 弧狀部524及弧狀部528。侧φ 512,係對應側面212,可 具有大約圓柱形的外形。狐狀部524,可滑㈣連接侧面 2 ’、頂面250 ’孤狀部528可滑順地連接側面512與相對 面540,弧狀部528可與擾拌容器1〇〇的内底面134呈銳 角S4。弧狀部528可為引入部2〇2的一例。 底部530包含相對面54〇及溝Μ2。在此,「底部」係 指較垂直於自轉轴Α4並包含授拌子508的中心之平面Ρ, 13 200948469 更靠近相對面540侧的部分。相對面54〇,係於底部530 中’相對於攪拌容器的内底面134,相對面540可為 平坦面。藉此,相對面54〇係藉由内底面134與相對面54〇 之間的接觸滑動,磨潰攪拌物20中所包含的凝集物24, 直到分散為初級粒子22為止。相對面54〇可為磨潰部2〇〇 的一例0 溝542,可於底部53〇中,形成於攪拌子5〇8的底面。 φ 溝542可為橫亙徑向的全長而延伸的直線形狀,例如, 溝542的寬度w可為約500私m,溝542的深度D可為約 5〇〇/zm。溝542可被配置成通過底面的中心,藉此,於底 °卩53〇中,在攪拌子508的底面形成一對的相對面540。 溝542可為引入部2G2的—例。溝542,具有溝壁部544、 溝傾斜部546及溝傾斜部548。溝壁部544可具有匚字形 的剖面’溝傾斜部5钧與溝傾斜部548可為連接溝壁部544 的開放端的兩端與相對面54〇的平面。溝傾斜部W與溝 魯傾斜4 548,係與授拌容器1〇〇的内底面134呈銳角幻。 溝542的配置位置不限於底面,亦可被配置於侧面512或 外周傾斜部214。 接著’使用第5圖來說明磨潰凝集物24的機構。授拌 係邊自轉,一邊於攪拌容器100内作接觸滑動。 此時,授拌子508係經由内底面134與弧狀部528之間的 間隙,將擾拌物20引入内底自134與相對面54〇之間的間 隙在此,所謂的撥拌子508將擾拌物20「引入」,不限 於藉由授拌子谓的自轉,使授拌物向授拌子的附 14 200948469 近靠近的情況。當攪拌子508於内底面134上作接觸滑動 時,通過存在於攪拌子5〇8的行進方向的攪拌物2〇之上的 情況,亦包含於「引入」。再者,藉由攪拌容器1〇〇内的攪 拌物20的流動,攪拌物2〇與攪拌子5〇8衝撞或接近的情 況’亦包含於「引入」。 因弧狀部528係滑順地連接侧面5 12與相對面54〇,底 部530與内底面134之間的間隙,隨著從側面512向相對 面54〇漸漸變窄。因祖對面540連接於弧狀部528,凝集 物24無法直接進入(鑽進)内底面134與相對面54〇的間 隙。攪拌物20中雖包含各種大小的凝集物24,但凝集物 24僅可接近相對面54〇至對應其大小的位置為止,凝集物 24被引入内底面134與弧狀部528,隨著向相對面前 ' 進,凝集物24漸漸地被瓦解而漸漸地變小。 通過内底面134與弧狀部528之間的間隙,被引入内 底面134與相對面54〇之間的間隙的凝集物24,藉由内底 Φ 面134與相對面540之間的接觸滑動,而被磨潰並瓦解。 因凝集物24是初級粒子22凝集而形成,凝集物24會被分 散至初級粒子22為止。若根據以上的構成,可使被引入相 對面540時的凝集物24的大小一致,可抑制力量被施加於 一處而使初級粒子22被粉碎這樣的情況。 在此’例如’公轉容器14〇的自轉轴A2向公轉轴A1 側傾斜時,旋轉部丨〇4係對攪拌子5〇8賦予將攪拌子5〇8 的相對面540向攪拌容器100的内底面134推壓之推壓力 F3。藉此,攪拌子5〇8 一邊向内底面134被推壓,一邊於 15 200948469 攪拌容器1〇〇内作接觸滑動。其結果,增加相對面54〇磨 潰凝集物24的力量。再者,攪拌子5〇8可於攪拌容器1〇〇 内安定並在内底面上作接觸滑動。 另外,攪拌子508亦將攪拌物20引入内壁面124與弧 狀部524之間。被引入的攪拌物2〇中所包含的凝集物24 一邊漸漸地瓦解變小,一邊被引入側面512與内壁面124 之間的間隙。攪拌子508亦可藉由側面512與内壁面124 若將攪拌子508The opposite face 240 is disposed relative to the inner bottom surface 134 of the mixing container (10) when the agitator 1〇8 is placed in the agitating vessel 1〇〇. As shown in the first bucket diagram, the opposing face 240 can be a flat face. The opposite face 24() can be an example of a worn portion. The top surface 250 is configured for agitation? The relative positions of the opposite faces 24 of 1 〇 8 ° top surface 25G may also be arranged approximately parallel to the opposing faces 24G. The fifth circle shows the stirrer 5G8 of another embodiment. Fig. 5 is a cross-sectional view showing the state in which the pulverizer 508 is cut in the vicinity of the center of the (four) sub-axis in the direction of the rotation axis A4. Fig. 5 is a view showing that the mixture 2G and the scrambler 5〇8 are placed in the mixing container. _ The outline of the state in which the drop container 100 is rotated by the rotating portion (10). First, an example of the configuration of the stirrer 508 will be described. The holders are 5〇8 with outer peripheral surface 510, bottom Μη 3® TS work, low "Ί 530 and top surface 25〇. The outer peripheral surface 51A is extended in the direction of the rotation axis Α4 of the agitating member 5〇8 corresponding to the outer peripheral surface 2Η) ′ to form the connectable top surface 250 and the opposite surface 54〇. The outer peripheral surface 51A includes a side surface, an arcuate portion 524, and an arc portion 528. Side φ 512, corresponding to side 212, may have an approximately cylindrical shape. The fox 524 is slidable (four) connecting the side 2', and the top surface 250' is slidably connected to the side surface 512 and the opposite surface 540, and the arc portion 528 can be formed with the inner bottom surface 134 of the spoiler container 1 Sharp angle S4. The arc portion 528 may be an example of the introduction portion 2〇2. The bottom 530 includes opposing faces 54 and gullies 2. Here, "bottom" refers to a plane 较 which is perpendicular to the rotation axis 并4 and which contains the center of the mixer 508, and 13 200948469 is closer to the side of the opposite surface 540 side. The opposite face 54 is in the bottom 530 'with respect to the inner bottom surface 134 of the agitating vessel, and the opposing face 540 can be a flat face. Thereby, the opposing surface 54 is slid by the contact between the inner bottom surface 134 and the opposing surface 54A, and the aggregate 24 contained in the agitating material 20 is pulverized until it is dispersed into the primary particles 22. The opposing surface 54A may be an example 0 groove 542 of the pulverizing portion 2A, and may be formed on the bottom surface of the stirring element 5〇8 in the bottom portion 53〇. The φ groove 542 may have a linear shape extending over the entire length of the transverse direction. For example, the width w of the groove 542 may be about 500 ng, and the depth D of the groove 542 may be about 5 〇〇/zm. The groove 542 may be configured to pass through the center of the bottom surface, whereby a pair of opposing faces 540 are formed on the bottom surface of the agitator 508 in the bottom 卩 53 。. The groove 542 may be an example of the introduction portion 2G2. The groove 542 has a groove wall portion 544, a groove inclined portion 546, and a groove inclined portion 548. The groove wall portion 544 may have a U-shaped cross section. The groove inclined portion 5 and the groove inclined portion 548 may be a plane connecting the both ends of the open end of the groove wall portion 544 and the opposite surface 54. The groove inclined portion W and the groove inclination 4 548 are sharply angled with the inner bottom surface 134 of the mixing container 1〇〇. The arrangement position of the groove 542 is not limited to the bottom surface, and may be disposed on the side surface 512 or the outer circumference inclined portion 214. Next, the mechanism for grinding the aggregate 24 will be described using Fig. 5. The mixing system rotates while making contact sliding in the agitating vessel 100. At this time, the mixing 508 is introduced into the gap between the inner bottom 134 and the opposite surface 54 by the gap between the inner bottom surface 134 and the curved portion 528. Here, the so-called dialing 508 is used. The "introduction" of the scrambled material 20 is not limited to the case where the agitating material is brought close to the feeder 14 200948469 by the rotation of the stirrer. When the agitator 508 is contact-sliding on the inner bottom surface 134, it is also included in the "introduction" by the presence of the agitating material 2〇 in the traveling direction of the agitating member 5〇8. Further, by the flow of the agitator 20 in the agitating vessel 1 , the case where the agitator 2 冲 collides with or approaches the agitator 5 〇 8 is also included in the "introduction". Since the arcuate portion 528 smoothly connects the side surface 51 and the opposite surface 54, the gap between the bottom portion 530 and the inner bottom surface 134 gradually narrows from the side surface 512 to the opposite surface 54. Since the opposite side 540 of the ancestor is connected to the arcuate portion 528, the agglomerate 24 cannot directly enter (drill) the gap between the inner bottom surface 134 and the opposite surface 54. Although the agitate 20 contains aggregates 24 of various sizes, the aggregate 24 can only approach the opposite surface 54〇 to a position corresponding to its size, and the aggregate 24 is introduced into the inner bottom surface 134 and the curved portion 528, as the opposite direction In the front, the agglomerate 24 gradually disintegrated and gradually became smaller. By the gap between the inner bottom surface 134 and the arcuate portion 528, the agglomerate 24 introduced into the gap between the inner bottom surface 134 and the opposite surface 54 is slid by the contact between the inner bottom Φ surface 134 and the opposite surface 540. It was crushed and disintegrated. Since the aggregate 24 is formed by aggregation of the primary particles 22, the aggregates 24 are dispersed to the primary particles 22. According to the above configuration, the size of the aggregates 24 when they are introduced into the opposite faces 540 can be made uniform, and it is possible to suppress the force from being applied to one place and the primary particles 22 to be pulverized. When the rotation axis A2 of the "revolving container 14" is inclined toward the revolution axis A1 side, for example, the rotating portion 丨〇4 applies the opposing surface 540 of the stirring element 5〇8 to the stirring container 100 to the stirring element 5〇8. The pressing force F3 is pressed by the bottom surface 134. Thereby, the agitating member 5〇8 is pressed against the inner bottom surface 134, and is in contact with the inside of the stirring container 1 15 15 200948469. As a result, the force of the opposing surface 54 is attenuated by the agglomerate 24. Further, the stirrer 5〇8 can be stabilized in the stirring vessel 1〇〇 and made to contact and slide on the inner bottom surface. In addition, the agitator 508 also introduces the agitator 20 between the inner wall surface 124 and the arcuate portion 524. The agglomerates 24 contained in the introduced agitator 2 are gradually disintegrated and become introduced into the gap between the side surface 512 and the inner wall surface 124. The stirrer 508 can also pass through the side 512 and the inner wall surface 124 if the stirrer 508
之間的接觸滑動,磨潰凝集物24。例如 適用於攪拌裝置10,即可提供一種攪拌方法,其具備:將 攪拌物20與攪拌子508置入攪拌容器中的步驟、以及藉由 旋轉邛104使攪拌容器1〇〇旋轉的步驟。在該攪拌方法的 使授拌容胃1GG旋轉的步驟中,將授拌物引人内底面134 ”弧狀。卩528之間’並藉由内底面ι34與相對面54〇之間 的接觸滑動,磨潰攪拌物2〇中所包含的凝集物24。 第6圖係表示溝的剖面形狀的另外的例。溝642具有 溝壁部644、溝傾斜部646及溝傾斜部648❹溝壁部料4具 予t的面。溝傾斜部646與溝傾斜部“8 ,可滑順 地結合溝壁部644的開放端的兩端與相對面54〇。 第7圖係表示溝的剖面形狀的另外的例。溝742具有 傾斜4 746及溝傾斜部748。溝傾斜部,係相對於相 對面540’可為傾斜面;;冓傾斜部748,係相對於溝傾斜部 6且相對於相對面54〇可為傾斜面。溝傾斜面7邨與溝 頃斜。Ρ 748係於一側的端部互相結合。溝傾斜部與溝 斜748的另一侧的端部係與相對面540、结合,形成剖 16 200948469 面為V字形或三角形的溝742。 第8圖係表示攪拌子5〇8的溝的平面形狀的另外的例 的底面圖。攪拌子508亦可具有圓弧形狀的溝842,溝842 的配置’其複數的溝842可被配置成從底面的中心向外側 擴大。溝842可被配置成在底面的中心附近形成相對面 540 ’溝842 ’可被配置成其從圓弧的内侧向外側的方向R1 與攪拌子508的旋轉方向r2大約相同。藉此,溝842係成 為容易引入擾拌物20。溝842可延伸至底面的中心附近為 ® 止,溝842亦可於底面的中心附近與其他的溝連接。 第9圖係表示攪拌子508的溝的平面形狀的另外的例 的底面圖。授拌子508,可具有圓弧形狀的溝942。溝942, 亦可被配置成其從圓弧的内側向外側的方向R1與溝842 • 逆向。Sliding between the contacts, the agglomerate 24 is abraded. For example, in the case of the stirring device 10, a stirring method may be provided which includes a step of placing the agitating member 20 and the agitating member 508 in the stirring vessel, and a step of rotating the agitating vessel 1 by the rotary crucible 104. In the step of rotating the mixing chamber 1GG of the stirring method, the feeding material is introduced into the inner bottom surface 134 "arc. Between 528" and slides by contact between the inner bottom surface ι34 and the opposite surface 54〇. The agglomerate 24 contained in the mixture 2 is crushed. Fig. 6 is a view showing another example of the cross-sectional shape of the groove. The groove 642 has a groove wall portion 644, a groove inclined portion 646, and a groove inclined portion 648. The four inclined faces 646 and the groove inclined portion "8 are slidably coupled to both ends of the open end of the groove wall portion 644 and the opposing faces 54". Fig. 7 is a view showing another example of the cross-sectional shape of the groove. The groove 742 has a slope 4 746 and a groove inclined portion 748. The inclined groove portion may be an inclined surface with respect to the opposite surface 540'; the inclined portion 748 may be an inclined surface with respect to the groove inclined portion 6 and with respect to the opposing surface 54. The ditch slope surface 7 village and the ditch are inclined. Ρ 748 is joined to each other at the ends of one side. The groove inclined portion and the other end portion of the groove 748 are joined to the opposing surface 540 to form a groove 742 having a V-shaped or triangular shape. Fig. 8 is a bottom view showing another example of the planar shape of the groove of the stirrer 5〇8. The agitator 508 may also have a circular arc shaped groove 842, the plurality of grooves 842 of which the arrangement of the grooves 842 may be arranged to expand outward from the center of the bottom surface. The groove 842 may be configured to form an opposite face 540' near the center of the bottom surface. The groove 842' may be configured such that its direction R1 from the inner side to the outer side of the circular arc is approximately the same as the rotational direction r2 of the agitating member 508. Thereby, the groove 842 is formed to easily introduce the scrambler 20. The groove 842 can extend to the vicinity of the center of the bottom surface as a stop, and the groove 842 can also be connected to other grooves near the center of the bottom surface. Fig. 9 is a bottom view showing another example of the planar shape of the groove of the agitating member 508. The mixer 508 may have a groove 942 having an arc shape. The groove 942 may be arranged such that it is reversed from the inner side to the outer side of the arc R1 and the groove 842.
第1 〇圖係表不攪拌子508的溝的平面形狀的另外的例 的底面圖授样子508,亦可具有複數條直線形狀的溝 1042溝1〇42的配置,其複數條溝1〇42可被配置成放射 狀溝1042 ’可被配置成在底面的中心附近形成相對面 溝1042可延伸至底面的中心附近為止。溝1 θα亦可 於底面的中心附近與其他的溝連接。 第11圖係表不攪拌子508的溝的平面形狀的另外的例 的底面圖授拌子5G8亦可有具有與授拌子同心的螺 線形狀的溝1142。溝1142 ’可被配置成其從螺線的内側向 的方向R3 ’與撲拌子5()8的旋轉方向大約相同。 藉此’將凝集物24取入溝的内部變得容易。溝1142,亦 17 200948469 可被配置成其從螺線的外側向内側的方向R4,與攪拌子 508的旋轉方向R2大約相同。 第12圖係表示另外的實施形態的攪拌子12〇8的剖面 圖。第12圖係表示將攪拌子12〇8於攪拌子12〇8的中心附 近向自轉軸A4方向切斷的情況。第12圖係表示將攪拌物 20與攪拌子1208置入攪拌容器1〇〇中,然後藉由旋轉部 104使擾拌谷器1 〇〇旋轉的狀態的概要。第13圖係表示本 實施形態的攪拌子1208的底面圖的一例。以下,使用第 ® 12圖與第13圖來說明攪拌子12〇8。 如同圖所示’攪拌子1208具備相對面1240、頂面1250 及中心孔1260。相對面1240與頂面1250,分別相當於授 拌子508的相對面540與頂面250,相對面1240係被配置 成相對於内底面134,頂面1250係被配置成相對於相對面 1240。攪拌子1208可於中心部具備中心孔1260。中心孔 1260可被配置成貫通相對面1240與頂面1250,中心孔 鲁 1260 ’可被配置成其中心孔1260的中心,位於自轉軸A4 的附近。藉此,攪拌子1208可具有甜甜圈的外形。 中心孔1260包含中心孔傾斜部1262、中心孔傾斜部 1264及内周面1266。中心孔傾斜部1262係被配置於中心 孔1260的頂面1250側的端部,中心孔傾斜部1262係連接 内周面1266與頂面1250。中心孔傾斜部1264係被配置於 中心孔1260的相對面1240側的端部,中心孔傾斜部1264 係連接内周面1266與頂面1250。中心孔傾斜部1262與中 心孔傾斜部1264,係沿著自轉轴A4,分別隨著向頂面1250In the first diagram, the bottom view of the planar shape of the groove of the stirrer 508 is not shown, and the groove 1042 of the plurality of straight grooves may be arranged, and the plurality of grooves 1〇42 may be arranged. It may be configured that the radial grooves 1042' may be configured to form an opposing face groove 1042 near the center of the bottom surface that extends to near the center of the bottom surface. The groove 1 θα may be connected to other grooves near the center of the bottom surface. Fig. 11 is a view showing another example of the planar shape of the groove of the agitating member 508. The bottom surface of the mixer 5G8 may have a spiral groove 1142 having a concentric shape with the stirrer. The groove 1142' may be configured such that its direction R3' from the inner side of the spiral is about the same as the direction of rotation of the puffing piece 5() 8. Thereby, it is easy to take the aggregate 24 into the inside of the groove. The groove 1142, also 17 200948469, may be arranged such that its direction R4 from the outer side to the inner side of the spiral is approximately the same as the direction of rotation R2 of the agitator 508. Figure 12 is a cross-sectional view showing a stirrer 12〇8 of another embodiment. Fig. 12 is a view showing a state in which the agitator 12〇8 is cut in the direction of the rotation axis A4 in the vicinity of the center of the agitator 12〇8. Fig. 12 is a view showing an outline of a state in which the agitator 20 and the agitator 1208 are placed in the agitating vessel 1 and the scrambler 1 is rotated by the rotating portion 104. Fig. 13 is a view showing an example of a bottom view of the agitator 1208 of the present embodiment. Hereinafter, the stirrer 12〇8 will be described using the Fig. 12 and Fig. 13 . As shown in the figure, the agitator 1208 has an opposing surface 1240, a top surface 1250, and a center hole 1260. Opposite face 1240 and top face 1250 correspond to opposing faces 540 and top face 250 of feeder 508, respectively, and opposing face 1240 is configured relative to inner bottom face 134, and top face 1250 is configured relative to opposing face 1240. The agitator 1208 can have a central bore 1260 at the center. The central bore 1260 can be configured to extend through the opposing face 1240 and the top face 1250, and the central bore 1260' can be configured as the center of its central bore 1260, adjacent the axis of rotation A4. Thereby, the stirrer 1208 can have the shape of a donut. The center hole 1260 includes a center hole inclined portion 1262, a center hole inclined portion 1264, and an inner peripheral surface 1266. The center hole inclined portion 1262 is disposed at an end portion on the top surface 1250 side of the center hole 1260, and the center hole inclined portion 1262 is connected to the inner peripheral surface 1266 and the top surface 1250. The center hole inclined portion 1264 is disposed at an end portion on the opposite surface 1240 side of the center hole 1260, and the center hole inclined portion 1264 connects the inner peripheral surface 1266 and the top surface 1250. The central hole inclined portion 1262 and the central hole inclined portion 1264 are along the rotation axis A4, respectively, along the top surface 1250
1S 200948469 側或相對面1240側而增加内徑。 中'^孔1260可為引入部202的一例。亦即,授拌子12〇8 可經由中心孔1260而將攪拌物2〇引入内底面134與相對 面1240之間的間隙,藉由内底面134與㈣φ 124〇 & $ 的接觸滑動,磨潰攪拌物2〇中所包含的凝集物24。另外, 即使是此情況,例如,公轉容器140的自轉轴Α2向公轉轴 八!侧傾斜時,旋轉部1〇4係對攪拌子12〇8賦予將攪拌子 1208的相對面124〇向攪拌容器1〇〇的内底面134推壓之 推壓力F3。攪拌子1208亦與攪拌子508相同地,亦可具 有溝542等。 ' 第14圖係表示本實施形態的攪拌子14〇8的侧面圖的 一例。第15圖係表示本實施形態的攪拌子14〇8的底面圖 ' 的一例。以下,使用笫14圖與第15圖來說明攪拌子14〇8。 攪拌子1408可於側面512具有溝1416,溝1416的剖面形 狀與平面形狀,可形成與溝542相同。攪拌子14〇8可於底 Φ 面形成溝1442’溝丨442的剖面形狀亦可為圓弧狀,溝1442 的平面形狀亦可為從底面的内側向外侧擴大的形狀。溝 1442的平面形狀,例如,亦可為於一端連接的二圓弧與藉 由孤狀部528的端部包圍的形狀。溝1442可被配置於伴隨 著授摔子1408的自轉,容易引入攪拌物2〇的方向。藉此, 可將引入的授拌物2〇有效果地向底面的中心附近壓入。 [實施例1] 使·用包含銅粉與樹脂溶液的導電膠來確認本實施形態 19 200948469 的效果。銅粉係使用平均粒徑為12;(zm的銅粉。粒徑係以 濕式法計測。樹脂溶液係使苯氧基樹脂溶解於三甘醇二甲 醚中來調製。苯氧基樹脂係調整為重量%3〇% 。導電膠試 料係混合銅粉13.8g、樹脂溶液9 4cc、三甘醇二甲醚 來調製。攪拌容器1〇〇係使用聚丙烯製容量為15〇cm3的容 器。旋轉部104係使用行星式的旋轉裝置。將攪拌容器1〇〇 固定於公轉容器140,公轉容器14〇係設定成一邊以26irpm 作自轉,一邊以340rpm作公轉。 攪拌的效果,係將銅粉的分散度依據日本工業規格jis K5400的4.7.2線條法來評價。亦即,於顆粒規的溝中注入 充分攪拌後的試料,使用到刀裝入,於溝中形成厚度連續 的試料層。觀察試料層,讀取於試料面中,一溝中排列出 • 現三條以上10mm以上連續的線條之處的刻度,作為分散 度。單位以表示。分散度係數值越小,表示銅粉越充 分分散。攪拌前的導電膠試料係未分散,以可測定至ι〇〇 Ο 仁111為止的顆粒規,無法測定分散度。 在實施例1中,使用其侧面212的外徑為2〇111111,相對 面240與頂面250之間的厚度為1〇mm,材質為不鏽鋼的攪 拌子1〇8。實驗係以以下的步驟來進行。於攪拌容器 置入如上所述調整後的導電膠試料及攪拌子1〇8。將攪拌 容器1〇〇設置於旋轉部104,然後使旋轉部1〇4以預定的 速度旋轉。改變授拌時間,測定分散度。第i表中表示實 施例1的實驗結果。表中的分散度係以「顆粒」來記裁。 由第1表所示可知,隨著攪拌時間經過,「顆粒」變小,充 20 200948469 分分散。 [第1表] 實施, m 30 實施例2 比較例1 比較例 2 比較例3 比較例4 捅拌時閟 (分) 5 10 20 5 10 20 30 5 10 20 30 30 30 30 Cu粉 13.S ♦— —— **— *— 13.8 4— «— 樹脂溶液 (樹庙分量30¾〕 9.4 <— K <— 9.4 <— ·<— 溶« 5 <一 — 5 <— — — 4— 攪拌媒介 攪拌子 108 4— ·— 攪拌子 108 <— ♦— 無 .和 <— 球 一個 二傕 <— 三個 顆粒(B法) 70 55 40 35 90 80 50 40 90 90 95 75 80 85 75 [實施例2] 在實施例2中’使用其側面212的外徑為25rnm,相對 面240與頂面250之間的厚度為1〇mm,材質為不鏽鋼的攪 拌子108。其他的條件係與實施例!相同,進行實驗。第1 表中表示實施例2的實驗結果。如第i表所示可知 授拌時間經過,「顆粒」變小,充分分散。 接著’以未置入授拌子作為比較例i來進行 他的條件係與實施例1相同,進行實 其 概。第1表中表干卜 較例1的實驗結果。如第1表所示,即使授摔時間的經過 「顆粒」的值幾乎無變化。 過’ (比較例2) 21 200948469 接著,使用直徑10mm的氧化錯球作為比較例2來進 行實驗。攪拌容器10〇置入導電膠試料及一個氧化锆球。 授拌時間為三十分鐘。其他的條件係與實施例1相同。第 1表中表示比較例2的實驗結果《如第1表所示,即使攪 拌三十分鐘’「顆粒」的值與比較例1幾乎無變化。 (比較例3) 接著,使用二個直徑1〇mm的氧化锆球作為比較例3 來進行實驗。攪拌容器1〇〇置入導電膠試料及二個氧化锆 ® 球。其他的條件係與比較例2相同。第1表中表示比較例 3的實驗結果。如第丨表所示,即使攪拌三十分鐘,「顆粒」 的值與比較例1幾乎無變化。 (比較例4) 、 接著’使用二個直徑1 〇mm的氧化錯球作為比較例3 來進行實驗。攪拌容器100置入導電膠試料及三個氧化锆 球。其他的條件係與比較例2相同。第丨表中表示比較例 φ 4的實驗結果。如第1表所示,即使攪拌三十分鐘,「顆粒」 的值與比較例1幾乎無變化乂 第16圖中表示實驗結果的圖表。在比較例i至比較例 4中’即使攪拌三十分鐘,「顆粒」的值幾乎無變化。另一 方面在實施例1與實施例2中可知隨著授掉時間經過, 「顆粒」急劇地減少。根據以上結果,藉由本實施形態的 授拌裝置、授拌子及授拌方法,可使授拌物中所包含的凝 集物有效果地分散。特別是即使為包含粒徑為數微米至次 微米的初級粒子凝集而成的凝集物的樹脂溶液也可使凝 22 200948469 集物細緻地分散。藉此,可獲得一種可抑制於塗佈面上發 生顆粒’例如筋狀的塗佈不均的發生的樹脂溶液、導電膠 等。 以上’使用實施形態說明了本發明,但本發明的技術 範圍不限定於上述實施形態所記載的範圍。該業者顯然可 對於上述實施形態作多樣的變更或改良。由申請專利範圍 的S己載可知’作如此的變更或改良的形態’亦可被包含於 本發明的技術範圍中。 應留意申請專利範圍、說明書及圖式中所示的裝置、 系統、程式、及方法中的動作、順序、步驟與步驟等的各 處理的實行順序,並未特別明示「之前」、「先J等;又, 之前的處理的輸出不限於在之後的處理中使用,可依任意 的順序而實現。關於申請專利範圍、說明書及圖式中的動 作流程,即使為了說明方便而使用「首先」、「接著」等來 說明’但並非意指必須以此種順序來實施。 [產業上的利用可能性] 本發明可利用於使粒子分散於液體中的攪拌裝置、授 拌子或者攪拌方法的產業中,例如,可利用於製造出一種 使導電性粒子分散於有機聚合物材料中而成的導電膠的化 學工業領域中。 23 200948469 【圖式簡單說明】 第1圖係表不以垂直於水平方向的平面來切斷本實施 形態的授拌裝置10而得的剖面圖。 第2圖係表示攪拌容器100、攪拌子1〇8、公轉容器14〇 的旋轉運動的概要。 帛3 ®係表示本實施形態的擾拌子1G8的側面圖的一 例0 _ 第4圖係表示本實施形態的攪拌子108的底面圖的一 例。 第5圖係表示另外的實施形態的攪拌子5〇8。 第6圖係表示溝的剖面形狀的另外的例。 第7圖係表示溝的剖面形狀的另外的例。 第8圖係表示攪拌子5〇8的溝的平面形狀的另外的例 的底面圖。1S 200948469 Side or opposite side 1240 side increases internal diameter. The middle hole 1260 may be an example of the introduction portion 202. That is, the stirrer 12〇8 can introduce the agitating material 2〇 into the gap between the inner bottom surface 134 and the opposite surface 1240 via the central hole 1260, and the inner bottom surface 134 and the (4) φ 124〇& $ contact sliding, grinding The agglomerate 24 contained in the mixture 2 is stirred. In addition, even in this case, for example, the rotation axis 2 of the revolution container 140 is turned to the revolution axis eight! When the side is inclined, the rotating portion 1〇4 applies a pressing force F3 to the agitating member 12〇8 to press the opposing surface 124 of the agitating member 1208 against the inner bottom surface 134 of the agitating vessel 1A. The stirrer 1208 is also the same as the stirrer 508, and may have a groove 542 or the like. Fig. 14 is a view showing an example of a side view of the agitator 14〇8 of the present embodiment. Fig. 15 is a view showing an example of the bottom view ' of the agitator 14 8 of the present embodiment. Hereinafter, the stirrer 14〇8 will be described using the 笫14 diagram and the fifteenth diagram. The agitator 1408 can have a groove 1416 on the side 512. The groove 1416 has a cross-sectional shape and a planar shape, and can be formed in the same manner as the groove 542. The agitating fins 14A8 may form a groove 1442' in the bottom Φ surface. The cross-sectional shape of the groove 442 may be an arc shape, and the planar shape of the groove 1442 may be a shape that expands from the inner side to the outer side of the bottom surface. The planar shape of the groove 1442 may be, for example, a shape in which two arcs connected at one end and an end portion of the solute portion 528 are surrounded. The groove 1442 can be disposed in a direction in which the agitating object 2〇 is easily introduced accompanying the rotation of the throwing member 1408. Thereby, the introduced cocktail 2 can be effectively pressed into the vicinity of the center of the bottom surface. [Example 1] The effect of the present embodiment 19 200948469 was confirmed by using a conductive paste containing copper powder and a resin solution. The copper powder used had an average particle diameter of 12; (zm copper powder. The particle size was measured by a wet method. The resin solution was prepared by dissolving a phenoxy resin in triethylene glycol dimethyl ether. The composition was adjusted to a weight % of 3% by weight. The conductive rubber sample was prepared by mixing 13.8 g of copper powder, 94 cc of a resin solution, and triethylene glycol dimethyl ether. The stirring vessel 1 was a container having a capacity of 15 〇cm 3 made of polypropylene. A planetary rotating device was used for the rotating portion 104. The stirring container 1 was fixed to the revolution container 140, and the revolution container 14 was set to rotate at 340 rpm while rotating at 26 μrpm. The effect of stirring was copper powder. The degree of dispersion was evaluated according to the 4.7.2 line method of Japanese Industrial Standard jis K5400. That is, the sample which was sufficiently stirred was injected into the groove of the particle gauge, and was placed in a blade to form a sample layer having a continuous thickness in the groove. Observe the sample layer and read it in the sample surface. The scales of three or more continuous lines of 10 mm or more are arranged in a groove as the dispersion. The unit is expressed. The smaller the dispersion coefficient value, the more sufficient the copper powder is. Dispersion The conductive paste sample was not dispersed, and the particle size up to the oxime 111 was measured, and the degree of dispersion could not be measured. In Example 1, the outer diameter of the side surface 212 was 2〇111111, and the opposite surface 240 was used. The thickness between the top surface 250 is 1 mm, and the material is stainless steel stirrer 1 〇 8. The experiment is carried out in the following steps. The conductive paste sample and the stirrer adjusted as described above are placed in the stirring vessel. 8. The stirring vessel 1 is placed in the rotating portion 104, and then the rotating portion 1〇4 is rotated at a predetermined speed. The mixing time is changed to measure the degree of dispersion. The experimental results of Example 1 are shown in Table i. The degree of dispersion is recorded by "particles." As shown in the first table, as the stirring time elapses, the "particles" become smaller, and the charge is dispersed in 2009. The first table is implemented, m 30 Example 2 Comparative Example 1 Comparative Example 2 Comparative Example 3 Comparative Example 4 捅 (minutes) 5 10 20 5 10 20 30 5 10 20 30 30 30 30 Cu powder 13.S ♦ — —— ** — *— 13.8 4— «—Resin solution (tree temple component 303⁄4) 9.4 <- K <- 9.4 <- · ·lt ;—Solution « 5 <1—5<--- 4— Stirring medium stirrer 108 4—·—Stirring 108 <- ♦ — No. and < — Ball One 傕 < — Three granules (Method B) 70 55 40 35 90 80 50 40 90 90 95 75 80 85 75 [Embodiment 2] In Embodiment 2, the outer diameter of the side surface 212 is 25 rnm, and between the opposite surface 240 and the top surface 250 The stirrer 108 is made of stainless steel and has a thickness of 1 mm. Other conditions and examples! The same, experiment. The experimental results of Example 2 are shown in Table 1. As shown in the table i, it can be seen that the "particles" become smaller and more dispersed. Then, the conditions in which the stir-mixer was not placed as the comparative example i were carried out in the same manner as in the first embodiment, and the details were ascertained. The results in Table 1 are compared with those in Example 1. As shown in the first table, there is almost no change in the value of "particles" even after the passing time. ('Comparative Example 2) 21 200948469 Next, an experiment was conducted using Comparative Oxidation Ball of 10 mm in diameter as Comparative Example 2. The stirring vessel 10 was placed in a conductive rubber sample and a zirconia ball. The mixing time is 30 minutes. Other conditions are the same as in the first embodiment. In the first table, the experimental results of Comparative Example 2 are shown. "As shown in Table 1, even if the stirring is for 30 minutes, the value of "particles" hardly changes from Comparative Example 1. (Comparative Example 3) Next, experiments were carried out using two zirconia balls having a diameter of 1 mm as Comparative Example 3. The stirring vessel 1 was placed in a conductive rubber sample and two zirconia balls. The other conditions are the same as in Comparative Example 2. The experimental results of Comparative Example 3 are shown in Table 1. As shown in the table, even if it was stirred for 30 minutes, the value of "particles" was almost unchanged from that of Comparative Example 1. (Comparative Example 4) Next, experiments were carried out using two oxidized wrong spheres having a diameter of 1 mm as Comparative Example 3. The stirring vessel 100 was placed with a conductive rubber sample and three zirconia balls. The other conditions are the same as in Comparative Example 2. The experimental results of Comparative Example φ 4 are shown in the third table. As shown in the first table, even if the mixture was stirred for 30 minutes, the value of "particles" hardly changed from that of Comparative Example 1. The graph showing the experimental results is shown in Fig. 16. In Comparative Example i to Comparative Example 4, the value of "particles" hardly changed even if it was stirred for thirty minutes. On the other hand, in the first embodiment and the second embodiment, it is understood that the "particles" sharply decrease as the transfer time elapses. According to the above results, the aggregating material contained in the raw material mixture can be effectively dispersed by the mixing device, the stirrer, and the mixing method of the present embodiment. In particular, even if it is a resin solution containing agglomerates in which primary particles having a particle diameter of several micrometers to a few micrometers are aggregated, the aggregates can be finely dispersed. Thereby, a resin solution, a conductive paste, or the like which can suppress the occurrence of uneven coating of particles such as ribs on the coated surface can be obtained. The present invention has been described above using the embodiments, but the technical scope of the present invention is not limited to the scope described in the above embodiments. It is obvious that the manufacturer can make various changes or improvements to the above embodiments. It is also known that the form of such a change or improvement is also included in the technical scope of the present invention. The order of execution of the processes, sequences, steps, and steps in the devices, systems, programs, and methods shown in the claims, the description, and the drawings is not specifically described as "before" or "first" In addition, the output of the previous processing is not limited to use in subsequent processing, and can be implemented in any order. Regarding the operation flow in the patent scope, the specification, and the drawing, even if it is convenient for explanation, "first" is used. "Next" and the like to illustrate 'but does not mean that it must be implemented in this order. [Industrial Applicability] The present invention can be utilized in an industry of a stirring device, a stirrer or a stirring method for dispersing particles in a liquid, and for example, can be used to produce a conductive particle dispersed in an organic polymer. The conductive adhesive made of materials is in the chemical industry. 23 200948469 [Brief Description of the Drawings] Fig. 1 is a cross-sectional view showing the feeding device 10 of the present embodiment not cut in a plane perpendicular to the horizontal direction. Fig. 2 is a view showing the outline of the rotational movement of the stirring container 100, the stirring unit 1〇8, and the revolution container 14〇.帛3® shows an example of a side view of the stirrer 1G8 of the present embodiment. Fig. 4 shows an example of a bottom view of the stirrer 108 of the present embodiment. Fig. 5 is a view showing a stirrer 5〇8 of another embodiment. Fig. 6 is a view showing another example of the cross-sectional shape of the groove. Fig. 7 is a view showing another example of the cross-sectional shape of the groove. Fig. 8 is a bottom view showing another example of the planar shape of the groove of the stirrer 5〇8.
第9圖係表示攪拌子5〇8的溝的平面形狀的另外的例 的底面圖Q 第10圖係表示攪拌子508的溝的平面形狀的另外的例 的底面圖。 第11圖係表示攪拌子5Q8的溝的平面形狀的另外的例 的底面圖。 第12圖係表示另外的實施形態的攪拌子1208的剖面 圖。 第13圖係表示本實施形態的攪拌子1208的底面圖的 24 200948469 一例。 第14圖係表示本實施形態的攪拌子1408的侧面圖的 一例。 第15圖係表示本實施形態的攪拌子1408的底面圖的 一例。 第圖係表示實驗結果的圖表。 【主要元件符號說明1 ❹ 10 :攪拌装置 20 : 攪拌物 22 :初級粒子 24 : 凝集物 100 :攪拌容器 104 :旋轉部 108 :攪拌子 110 :蓋部 112 :周壁部 114 :底板部 116 :腳輪 118 :内面 122 :外壁面 124 :内壁面 132:外底面 134 :内底面 140 :公轉容器 142 :筒壁部 144 :筒底部 146 :軸部 150 :曲柄 152 :軸承 154 :軸桿 156 .馬達 158 :平衡配重 160 :支持部 162 :腳部 200 :磨潰部 202 :引入部 210 .外周部 25 200948469Fig. 9 is a bottom view showing another example of the planar shape of the groove of the stirrer 5〇8. Fig. 10 is a bottom view showing another example of the planar shape of the groove of the stirrer 508. Fig. 11 is a bottom view showing another example of the planar shape of the groove of the agitating member 5Q8. Fig. 12 is a cross-sectional view showing a stirrer 1208 of another embodiment. Fig. 13 is a view showing an example of 24 200948469 of the bottom view of the stirrer 1208 of the present embodiment. Fig. 14 is a view showing an example of a side view of the agitator 1408 of the present embodiment. Fig. 15 is a view showing an example of a bottom view of the agitator 1408 of the present embodiment. The figure is a chart showing the results of the experiment. [Main component code description 1 ❹ 10 : Stirring device 20 : Stirring material 22 : Primary particle 24 : Aggregate 100 : Stirring container 104 : Rotating portion 108 : Stirrer 110 : Cover portion 112 : Peripheral wall portion 114 : Floor portion 116 : Caster 118: inner surface 122: outer wall surface 124: inner wall surface 132: outer bottom surface 134: inner bottom surface 140: revolution container 142: cylinder wall portion 144: cylinder bottom portion 146: shaft portion 150: crank 152: bearing 154: shaft 156. : balance weight 160 : support portion 162 : leg portion 200 : wear portion 202 : introduction portion 210 . outer peripheral portion 25 200948469
212 : 侧面 214 : 外周傾斜部 222 : 錐形部 224 : 弧狀部 226 : 錐形部 228 : 弧狀部 240 : 相對面 250 : 頂面 508 : 攪拌子 510 : 外周面 512 : 侧面 524 : 圓弧部 528 : 圓弧部 530 : 底部 540 : 相對面 542 : 溝 544 : 溝壁部 546 : 溝傾斜部 548 : 溝傾斜部 642 : 溝 644 : 溝壁部 646 : 溝傾斜部 648 : 溝傾斜部 742 : 溝 746 : 溝傾斜部 748 : 溝傾斜部 842 : 溝 942 : 溝 1042 :溝 1142 :溝 1208 :攪拌子 1240 :相對面 1250 :頂面 1260 :中心孔 1262 :中心孔傾斜部 1264 :中心孔傾斜部 1266 :内周面 1408 :攪拌子 1416 :溝 1442 :溝 26212 : side surface 214 : outer peripheral inclined portion 222 : tapered portion 224 : curved portion 226 : tapered portion 228 : curved portion 240 : opposite surface 250 : top surface 508 : stirring rod 510 : outer peripheral surface 512 : side surface 524 : round Arc portion 528: arc portion 530: bottom portion 540: opposite surface 542: groove 544: groove wall portion 546: groove inclined portion 548: groove inclined portion 642: groove 644: groove wall portion 646: groove inclined portion 648: groove inclined portion 742 : groove 746 : groove inclined portion 748 : groove inclined portion 842 : groove 942 : groove 1042 : groove 1142 : groove 1208 : stirring rod 1240 : opposite surface 1250 : top surface 1260 : center hole 1262 : center hole inclined portion 1264 : center Hole inclined portion 1266: inner peripheral surface 1408: stirrer 1416: groove 1442: groove 26
Claims (1)
Applications Claiming Priority (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
JP2008007451A JP4971207B2 (en) | 2008-01-16 | 2008-01-16 | Stirring apparatus, stirring bar, and stirring method |
Publications (2)
Publication Number | Publication Date |
---|---|
TW200948469A true TW200948469A (en) | 2009-12-01 |
TWI363657B TWI363657B (en) | 2012-05-11 |
Family
ID=40885251
Family Applications (1)
Application Number | Title | Priority Date | Filing Date |
---|---|---|---|
TW098101422A TW200948469A (en) | 2008-01-16 | 2009-01-15 | Stirring device, stirrer, and stirring method |
Country Status (4)
Country | Link |
---|---|
JP (1) | JP4971207B2 (en) |
CN (1) | CN101730579B (en) |
TW (1) | TW200948469A (en) |
WO (1) | WO2009090859A1 (en) |
Families Citing this family (8)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
ITBO20150192A1 (en) * | 2015-04-17 | 2016-10-17 | Alfa Srl | MIXER FOR FLUID PRODUCTS |
CN105381753B (en) * | 2015-12-04 | 2018-01-09 | 山东出入境检验检疫局检验检疫技术中心 | A kind of coal caking index measure agitating device |
CN109068880B (en) * | 2016-05-17 | 2020-12-04 | 雀巢产品有限公司 | Beverage preparation device |
JP6633506B2 (en) * | 2016-12-26 | 2020-01-22 | 大同化工株式会社 | Kneading device |
JP7041940B2 (en) * | 2017-10-23 | 2022-03-25 | 株式会社写真化学 | Rotation processing adapter |
CN110237755A (en) * | 2019-06-24 | 2019-09-17 | 中国工程物理研究院激光聚变研究中心 | A kind of polishing magnetorheological fluid stirs evenly sliding device |
DE102020127240B4 (en) | 2020-10-15 | 2022-05-19 | Fritsch Gmbh | Planetary mill with inclined planetary axis |
DE102020127239B4 (en) | 2020-10-15 | 2022-10-06 | Fritsch Gmbh | Planetary mill with cooling |
Family Cites Families (6)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
JPS60156538A (en) * | 1984-01-27 | 1985-08-16 | Imamura Seisakusho:Kk | Apparatus for stirring, mixing, and kneading of liquid or powder |
JPH0457238U (en) * | 1990-09-21 | 1992-05-15 | ||
JP2594213B2 (en) * | 1992-03-25 | 1997-03-26 | 株式会社奈良機械製作所 | Particulate material processing equipment |
JP3904819B2 (en) * | 2000-09-27 | 2007-04-11 | 株式会社リコー | Dispersion method and dispersion apparatus |
JP2003275555A (en) * | 2002-01-15 | 2003-09-30 | Sumitomo Bakelite Co Ltd | Mixing method and mixing device for solid and liquid materials |
JP4235888B2 (en) * | 2002-06-07 | 2009-03-11 | 日立化成工業株式会社 | Conductive paste |
-
2008
- 2008-01-16 JP JP2008007451A patent/JP4971207B2/en active Active
-
2009
- 2009-01-08 CN CN2009800003505A patent/CN101730579B/en active Active
- 2009-01-08 WO PCT/JP2009/000037 patent/WO2009090859A1/en active Application Filing
- 2009-01-15 TW TW098101422A patent/TW200948469A/en unknown
Also Published As
Publication number | Publication date |
---|---|
JP2009165970A (en) | 2009-07-30 |
TWI363657B (en) | 2012-05-11 |
WO2009090859A1 (en) | 2009-07-23 |
CN101730579B (en) | 2012-11-07 |
CN101730579A (en) | 2010-06-09 |
JP4971207B2 (en) | 2012-07-11 |
Similar Documents
Publication | Publication Date | Title |
---|---|---|
TW200948469A (en) | Stirring device, stirrer, and stirring method | |
TW201143881A (en) | Agitating and mixing apparatus and method for manufacturing resin composition for sealing semiconductor | |
JP6863211B2 (en) | Granulation manufacturing method and manufacturing equipment | |
JP2021003703A (en) | Dispersion mixing system with dispersion mixing pump used for slurry production | |
JP5360902B2 (en) | Particle polishing method and particle polishing system | |
CN206881631U (en) | A kind of efficient pulverizing agitating device of high stability | |
CN206853563U (en) | A kind of dispersion impeller | |
JPWO2007126048A1 (en) | Method for producing uniform and stable suspension and apparatus therefor | |
CN216396181U (en) | Medicine mixing arrangement | |
US9022640B2 (en) | Stirring apparatus for reducing vortexes | |
CN205340623U (en) | Take loading attachment's food processing mixer | |
CN205815543U (en) | A kind of mould wash mixer | |
CN201768504U (en) | Liquid-solid mixer | |
CN204380591U (en) | A kind of travelling mixer | |
CN208287903U (en) | A kind of pre-mixing apparatus of difference apparent density powder | |
CN207418308U (en) | A kind of mixer for being used for powdered activated carbon and adhesive | |
CN108556170A (en) | It is a kind of that there is the plastic stir device for shaking function | |
Nickerson et al. | Agitation and Particle Size Reduction Techniques | |
KR20160042716A (en) | Countinuous type powder mixer | |
CN220824720U (en) | Micro powder mixing and stirring device | |
CN218365808U (en) | A mixing apparatus for plastic pellet production | |
CN202890957U (en) | Automatic-mixing cosmetic container | |
CN203777962U (en) | Vertical powder stirrer | |
JP2672817B2 (en) | Mixing machine | |
CN211514342U (en) | Continuous mixer |