201111026 六、發明說明： 【發明所屬之技術領域】201111026 VI. Description of the invention: [Technical field to which the invention belongs]
本發一 ° ·— 有關於— 及方法。 【先前技術】This is a ° ° - related to - and method. [Prior Art]
法有過濾法、壓差過濾法、蒸發法 面活性劑法等。 過濾法是將混合物流經具有適當孔隙大小的遽網或遽 紙二以將其中的懸浮顆粒過遽在的渡網或I紙上。但是當 懸浮顆粒累積在濾網或濾紙的量增加到一定程度時，會使 ^過濾的速度變非常慢，而需更換濾網或濾紙。壓差過濾 法則是在濾網或濾紙的兩侧提供一壓力差，以增加過濾的 速度。 蒸發法是利用加熱或減壓，使混合物中的液體成分蒸 發成氣體而離開原本的混合物，從而達成分離液體與懸浮 顆粒的目的。但是蒸發法應用在液體含量過高的混合物 時，並不經濟。 離心分離法是利用在旋轉狀態下液體與固體懸浮顆粒 具有不同的離心力，而迫使懸浮顆粒沈澱下來。然後再將 液體與沈澱的顆粒分離。離心分離法通常適用在固體懸浮 顆粒的密度明顯大於液體的混合物中。例如在太陽能產業 中’為了將矽塊切割成片狀的矽晶圓（wafer)，通常使用線 201111026 鋸(wire saw)搭配碳化矽(SiC)研磨漿料進行切割， ， 的碳化矽研磨漿料，因摻雜有矽塊的碎削及雜 用過 物質），必須經過分離程序才能再回收利用。'質(例如含鐵 利用離心分離法來回收碳化矽研磨聚料。 時’通常是 氣泡-介面活性劑法是在夜態 人 介面活性劑（surfactant)，然後再 “ &物中加入微量的 氣體’並在液態混合物中形成翕^液態混合物的底部通入 >包。因 igdb wi, 活性劑，所形成的氣泡表面可 體中存在有介面 粒。當氣泡上升並浮到液態現合=液體混合物中的懸浮顆 再將附著有懸浮顆粒的泡沫移除。時會形成泡沫， 懸浮顆粒具有太高的密度時，队仁疋备液態混合物中的 匕方法並不適用。 【發明内容】 本發明之一目的係提供〜種 能分離一混合物中的固態顆粒與液^分離系統及方法，俾 本發明之另一目的係一種離、、八 增進離心分離系統之固態廢料的刀離系統及方法，俾能 離心分離系統之效能。 。收及清潔效率，以增進 根據上述目的，此離心分離 置、刮刀、中空連接器、漏斗c括旋轉桶、驅動裝 具有一中心軸以及一底部開口。器以及谷置桶8旋轉桶 中心軸為中心旋轉。刮刀配置於3動裝置可驅動旋轉桶以 旋轉桶内側之一物質，使該物二轉桶内部，用以刮除該 下。中空連接器位於旋轉桶下方錢轉桶之底部開口落 用以承接被刮刀刮除之物質。鬼、且與旋轉桶間隔一間隙， 辦斗承接器位於中空連接器 201111026 下方，以承接被刮刀刮除而由中空連接器落下之物質，漏 斗承接器之上緣與中空連接器之下緣的垂直間距為約5公 分至約80公分。容置桶位於該漏斗承接器下方，用以收集 經漏斗承接器落下之物質。 在一實施方式中，上述之漏斗承接器具有一上開孔， 且中空連接器具有一下開孔，其中漏斗承接器之上開孔的 面積大於中空連接器之下開孔的面積。在一實施例中，漏 斗承接器並具有一下開孔，且位在容置桶内。 鲁 本發明之另一態樣係提供一種離心分離方法5此方法 包括：（1)提供一離心分離器；（2)提供一漏斗承接器以及一 容置桶，其中該漏斗承接器置於該容置桶上；以及(3)將漏 斗承接器以及容置桶設置於離心分離器之中空連接器下 方，且該漏斗承接器之上緣與中空連接器之下緣的垂直間 距為約5公分至約80公分。其中該離心分離器包括如上所 述之驅動裝置、旋轉桶、刮刀以及中空連接器。 【實施方式】 本發明一實施方式之離心分離系統係用以將一混合物 (包含固態顆粒及液體）中的固態顆粒與液體分離，離心分 離系統是利用固體與液體的離心力差異，而達成分離固態 顆粒及液體的目的。請參照第1圖，其為本發明一實施方 式之離心分離系統100的剖面示意圖。離心分離系統100 主要包括驅動裝置110、旋轉桶120、刮刀130、中空連接 器140、漏斗承接器150以及容置桶160。 旋轉桶120具有一中心軸Ο以及一底部開口 122，且 201111026 旋轉桶120付二心軸〇為中心旋轉。在一實施例 轉桶120可大致=中空圓柱殼體。旋轉桶12〇可耥接至 驅動裝置11=轉=U2,並可經由驅_ ιι〇帶動而使 旋轉桶120說轉。在另一實施例中，驅動mi〇可為一 電動馬達，且配置在旋轉桶120的上方。 在一實施例中’離心分離系統100 1包括有進料管 180,且進料官180之-端由旋_ 12〇的底部心122延 伸進入旋轉桶12G的内部。進料管⑽主要用以將待分離 的混合物注入旋_ 120 _側側壁上。在本實施例中， =進料管⑽注人混合物時，旋轉桶12G是處於旋轉狀態。 :此’所注入的混合物因受離心力作用而不會立刻向下流 動0 第2圖繪示本發明-實施方式之旋轉桶12〇分離一現 合物中固體與液體的剖面示意圖。在-實施例中，旋轉桶 12〇包括圓柱側壁124以及一傾斜壁126。傾斜壁126連接 於圓柱侧壁124的下緣，並以一角度0向旋轉桶12〇的内 側傾斜。當進料管180朝向旋轉桶12〇的圓柱侧壁124注 入混合物時(如第2圖中箭頭Di所示），混合物因離心力作 用而滯留在圓枉侧壁124内側，並隨著圓柱側壁124 一起 旋轉。此時，混合物中的固態顆粒受離心力作用，會向圓 柱側壁124的方向移動（如第2圖中箭頭Vp所示），並沈積 在圓柱側壁124上而形成沈積物128。混合物中液體的部 分緩慢向下流動，並由傾斜壁126的下緣流出。因為混合 物中的液體部分仍受離心力作用，當液體部分離開倾斜壁 126的下緣時’會向旋轉桶120的外側方向離開，如第2 201111026 圖中箭頭D。所示。 在另一實施例中，在上述注入混合物之前，可以先注 入一溶劑（例如聚乙二醇’ PEG或其他溶劑）。所注入的溶 劑受離心力作用而滯留在圓柱側壁124内側，並隨著圓柱 側壁124 —起旋轉。當注入的溶劑填滿傾斜壁126上方的 空間之後’再注入欲進行分離的混合物’以進行離心分離 程序。 刮刀130配置於旋轉桶120内，用以刮除沈積在旋轉 ® 桶120内侧的沈積物，並使沈積物經由旋轉桶120的底部 開口 122落下。在一實施例中，當累積在旋轉桶120内侧 的沈積物質到達一定量時，使用刮刀130刮除沈積物。在 一實施例中，到刀130下方連接至一連桿132，且連桿132 耦接至一轉動機構134。因此，刮刀130能以連桿132為 轉軸而轉動。當欲進行刮除沈積物的程序時，首先停止進 料管180供給混合物進入旋轉桶120内，並降低旋轉桶12〇 的旋轉速度。然後轉動刮刀130使刮刀130與旋轉桶12〇 • 的内侧侧壁些微接觸。此時，旋轉桶120處於低速旋轉狀 態’所以可在不移動刮刀13〇的狀況下，將沈積在旋轉桶 120側壁上的沈積物刮除。被刮除的沈積物由旋轉桶ι2〇 的底部開口 122落下。當刮除沈積物完成後，可轉動刮刀 130使刮刀130離開旋轉桶12〇的侧壁，以接著繼續進行 分離程序。 中空連接器140位於旋轉桶12〇下方，以承接被刮刀 130刮除的沈積物。當刮刀13()刮除沈積物時，因旋轉桶 120處於旋轉狀態，所以被刮除的沈積物可能會朝各方向 201111026 中空連接器14G可限制沈義的_方向， 並避免被刮除的沈積物污染設備的其他部件。 140具有-下開孔144,被刮除的沈積物可經由中== 140的下開孔144落下。此外，+空遠 逆接器 12〇門隔a#絲 連接器WO與旋轉桶 120間^ 一間隙h，當旋轉桶12〇進行分離程序時 的液體部分可經由間隙h離開旋轉桶12〇β 刀The method includes a filtration method, a differential pressure filtration method, an evaporation method, and the like. The filtration method is to flow the mixture through a mesh or paper 2 having an appropriate pore size to pass the suspended particles therein to the web or I paper. However, when the amount of suspended particles accumulated in the filter or filter paper is increased to a certain extent, the filtration rate becomes very slow, and the filter or filter paper needs to be replaced. The differential pressure filtration method provides a pressure differential across the screen or filter to increase the rate of filtration. The evaporation method utilizes heating or decompression to evaporate the liquid component in the mixture into a gas and leave the original mixture, thereby achieving the purpose of separating the liquid and the suspended particles. However, the evaporation method is not economical when applied to a mixture having a high liquid content. The centrifugal separation method utilizes a centrifugal force different from that of the suspended solid particles in the rotating state to force the suspended particles to precipitate. The liquid is then separated from the precipitated particles. Centrifugal separation is generally suitable for use in mixtures where the density of solid suspended particles is significantly greater than that of liquids. For example, in the solar industry, in order to cut a crucible into a sheet-shaped wafer, a wire saw is used with a wire saw 20111026 with a cerium carbide (SiC) polishing slurry for cutting. , due to the inclusion of chopped pieces and miscellaneous substances, must be separated before they can be recycled. 'Quality (for example, iron-containing centrifugal separation method to recover the cerium carbide abrasive aggregate. When 'the bubble is usually the surfactant-surfactant method is in the night state human surfactant (surfactant), then add a small amount of & The gas 'and the bottom of the liquid mixture formed in the liquid mixture is passed into the package. Because of the igdb wi, the active agent, the surface of the bubble formed may have interfacial particles in the body. When the bubble rises and floats to the liquid state = The suspended particles in the liquid mixture are further removed by the foam to which the suspended particles are attached. When the foam is formed, and the suspended particles have a too high density, the method of preparing the liquid in the liquid mixture is not suitable. One object of the invention is to provide a solid particle and liquid separation system and method capable of separating a mixture, and another object of the invention is a knife separation system and method for removing solid waste from a centrifugal separation system. , the efficiency of the centrifugal separation system. The cleaning efficiency is increased to enhance the centrifugal separation, the scraper, the hollow connector, the funnel The barrel and the driving device have a central shaft and a bottom opening, and the central axis of the rotating barrel of the valley barrel 8 rotates. The scraper is arranged in the 3 moving device to drive the rotating barrel to rotate a substance inside the barrel to make the object rotate twice. The inside of the barrel is used to scrape the bottom. The hollow connector is located at the bottom of the rotating drum below the rotating bucket to take up the material scraped off by the scraper. The ghost is separated from the rotating bucket, and the bucket receiver is located in the hollow. Below the connector 201111026, to receive the material scraped off by the scraper and dropped by the hollow connector, the vertical distance between the upper edge of the funnel receiver and the lower edge of the hollow connector is about 5 cm to about 80 cm. Under the funnel receiver, the material falling through the funnel receiver is collected. In one embodiment, the funnel receiver has an upper opening, and the hollow connector has a lower opening, wherein the funnel receiver has an opening above the funnel The area is larger than the area of the opening below the hollow connector. In one embodiment, the funnel receiver has a lower opening and is located in the receiving barrel. The sample system provides a centrifugal separation method 5, the method comprising: (1) providing a centrifugal separator; (2) providing a funnel receiver and a receiving barrel, wherein the funnel receiver is placed on the receiving barrel; 3) The funnel receiver and the receiving barrel are disposed under the hollow connector of the centrifugal separator, and the vertical distance between the upper edge of the funnel receiver and the lower edge of the hollow connector is about 5 cm to about 80 cm. The centrifugal separator includes a driving device, a rotary drum, a doctor blade, and a hollow connector as described above. [Embodiment] A centrifugal separation system according to an embodiment of the present invention is for using solid particles in a mixture (including solid particles and liquid). Separating from the liquid, the centrifugal separation system utilizes the difference in centrifugal force between the solid and the liquid to achieve the purpose of separating the solid particles and the liquid. Referring to Fig. 1, there is shown a schematic cross-sectional view of the centrifugal separation system 100 according to an embodiment of the present invention. The centrifugal separation system 100 mainly includes a driving device 110, a rotary tub 120, a scraper 130, a hollow connector 140, a funnel receiver 150, and a receiving tub 160. The rotary tub 120 has a central shaft Ο and a bottom opening 122, and the 201111026 rotary drum 120 is rotated about the center of the shaft. In one embodiment, the drum 120 can be substantially = hollow cylindrical housing. The rotary tub 12 can be coupled to the drive unit 11 = turn = U2, and the rotary tub 120 can be rotated by the drive _ ιι. In another embodiment, the drive mi can be an electric motor and disposed above the rotating tub 120. In one embodiment, the centrifugal separation system 100 1 includes a feed tube 180, and the end of the feed register 180 extends from the bottom core 122 of the spin 12 into the interior of the rotating drum 12G. The feed pipe (10) is mainly used to inject the mixture to be separated into the side wall of the rotary _ 120 _. In the present embodiment, when the feed pipe (10) is injected into the mixture, the rotary tub 12G is in a rotating state. : The injected mixture does not immediately flow downward due to the centrifugal force. Fig. 2 is a schematic cross-sectional view showing the solid and liquid in the present embodiment of the rotating drum 12 of the present invention. In the embodiment, the rotating tub 12A includes a cylindrical side wall 124 and an inclined wall 126. The inclined wall 126 is coupled to the lower edge of the cylindrical side wall 124 and is inclined at an angle 0 toward the inner side of the rotary tub 12'. When the feed tube 180 injects the mixture toward the cylindrical side wall 124 of the rotating tub 12' (as indicated by the arrow Di in Fig. 2), the mixture stays inside the round side wall 124 due to the centrifugal force, and along with the cylindrical side wall 124 Rotate together. At this time, the solid particles in the mixture are subjected to centrifugal force and are moved toward the side wall 124 of the cylinder (as indicated by an arrow Vp in Fig. 2) and deposited on the side wall 124 of the cylinder to form a deposit 128. The portion of the liquid in the mixture flows slowly downward and exits from the lower edge of the inclined wall 126. Since the liquid portion of the mixture is still subjected to centrifugal force, when the liquid portion leaves the lower edge of the inclined wall 126, it will leave toward the outside of the rotary tub 120, as indicated by arrow D in the second 201111026 figure. Shown. In another embodiment, a solvent (e.g., polyethylene glycol 'PEG or other solvent) may be injected prior to the above injection of the mixture. The injected solvent is retained by the centrifugal force and is retained inside the cylindrical side wall 124 and rotates with the cylindrical side wall 124. After the injected solvent fills the space above the inclined wall 126, the mixture to be separated is re-injected to perform a centrifugation process. The scraper 130 is disposed in the rotating tub 120 for scraping deposits deposited inside the rotating tub 120 and allowing the deposit to fall through the bottom opening 122 of the rotating tub 120. In an embodiment, when the deposition material accumulated inside the rotary tub 120 reaches a certain amount, the scraper 130 is used to scrape off the deposit. In one embodiment, a link 132 is coupled to the lower portion of the blade 130, and the link 132 is coupled to a rotating mechanism 134. Therefore, the scraper 130 can be rotated with the link 132 as a rotating shaft. When the procedure for scraping the deposit is to be performed, the feed pipe 180 is first stopped to supply the mixture into the rotary tub 120, and the rotational speed of the rotary tub 12 is lowered. The scraper 130 is then rotated to bring the scraper 130 into slight contact with the inner side wall of the rotating tub 12'. At this time, the rotary tub 120 is in the low-speed rotation state so that the deposit deposited on the side wall of the rotary tub 120 can be scraped off without moving the scraper 13 。. The scraped deposit falls from the bottom opening 122 of the rotating bucket ι2〇. When the scraping of the deposit is completed, the scraper 130 can be rotated to cause the scraper 130 to exit the side wall of the rotating tub 12's to continue the separation process. The hollow connector 140 is located below the rotating tub 12 , to receive the deposit scraped off by the scraper 130. When the scraper 13 () scrapes off the deposit, since the rotating tub 120 is in a rotating state, the scraped deposit may be directed in all directions 201111026. The hollow connector 14G may limit the _ direction of the sinking and avoid being scraped. Sediment contaminates other parts of the equipment. The 140 has a lower opening 144, and the scraped deposit can fall through the lower opening 144 of the middle == 140. In addition, the + air remote reverser 12 door a # silk connector WO and the rotating tub 120 ^ a gap h, when the rotating bucket 12 〇 the separation process, the liquid portion can leave the rotating bucket 12 〇 β knife through the gap h
漏斗承接器150位於中空連接器14〇下方，以承 刮刀130刮除而由該中空連接器⑽落下之沈積物。在一 實施例中，該漏斗承接器具有一上開孔154，且漏斗承接 器150之上開孔154的面積大於中空連接器14〇之下開孔 144的面積。再者，漏斗承接器15〇的上緣152與中空連 接器140的下緣142的垂直間距d為約5公分至約8〇公 分。在一特定實施例中，垂直間距d為約1〇公分至約& 公分。存在間距d對於整體設備運作的方便性有助益，且 漏斗承接器150不宜與中空連接器14〇直接固定連接，下 文中將更詳細敘述。 容置桶160位於漏斗承接器15〇下方，以收集經漏斗 承接器150落下之沈積物。在一實施例中，該漏斗承接器 具有一下開孔156，且下開孔156位於容置桶160内。收 集在容置桶160内的沈積物通常具有高密度(例如密度約為 3000 Kg/m )，因此具有很大的重量。在一實施例中，容置 桶160之外表面具有兩環形凸緣162，以作為搬運容置桶 160的施力部位。在另一實施例中，容置桶16〇設置在一 棧板上（未圖示），可利用一機械設備將棧板、容置桶160 以及容置桶160上的漏斗承接器15〇快速移出。 201111026 接器150的上緣152與中空連接器140的下緣The hopper adapter 150 is located below the hollow connector 14 , to scrape the deposits that are scraped off by the squeegee 130 from the hollow connector (10). In one embodiment, the funnel receptacle has an upper opening 154 and the area of the opening 154 above the funnel receptacle 150 is greater than the area of the opening 144 below the hollow connector 14. Further, the vertical distance d between the upper edge 152 of the funnel receiver 15A and the lower edge 142 of the hollow connector 140 is from about 5 cm to about 8 cm. In a particular embodiment, the vertical spacing d is from about 1 centimeter to about & centimeters. The presence of the spacing d is helpful for the ease of operation of the overall apparatus, and the funnel receiver 150 is not intended to be directly fixedly coupled to the hollow connector 14A, as will be described in more detail below. The receiving tub 160 is located below the funnel receptacle 15〇 to collect deposits that have fallen through the funnel receptacle 150. In one embodiment, the hopper receptacle has a lower opening 156 and the lower opening 156 is located within the receiving tub 160. The deposits collected in the containment tub 160 typically have a high density (e.g., a density of about 3000 Kg/m) and therefore have a large weight. In one embodiment, the outer surface of the receiving tub 160 has two annular flanges 162 as a force applying portion for carrying the receiving tub 160. In another embodiment, the receiving bucket 16 is disposed on a pallet (not shown), and the pallet, the receiving tub 160, and the funnel receptacle 15 on the receiving tub 160 can be quickly assembled by using a mechanical device. Move out. 201111026 The upper edge 152 of the connector 150 and the lower edge of the hollow connector 140
斗承接==巨d可方便進行容置桶160的搬運。若漏 門=上緣152與中空連接器140的下緣142之 距d或疋間距d太小（例如小於約5公分），在利 =設備移動容置桶16〇以及漏斗承接器15〇時，可能 ㈣^接器Μ或容置桶16G)與中空連接器14G或附近 叙f發生碰撞或衝突，導致㈣設備本體或是容置桶⑽ ，。但若間距d太大(例如大於約8〇公分），當使用刮刀 。刮除沈積物時，被刮除的沈積物可能飛濺出漏斗承接 器150所能承接的範圍’而造成污染。此外，漏斗承接器 yo不宜直接固定連接在中空連接器14〇下方。因為在某 些應用中，被刮除的沈積物具黏著性，且會在空氣中硬化 而黏滞在漏斗承接H 15〇的表面上。若漏斗承接器15〇直 接固定在中空連接器140下方，可能因不易清潔而使漏斗 承接器150堵塞。 在另一實施例中’離心分離系統100更包括有一中空 容器170,且旋轉桶12〇位在中空容器170内。當旋轉桶 12〇進行分離程序時，被分離的液體經由間隙h離開旋轉 桶120後，可收集在中空容器170内。中空容器17〇的底 部可具有一斜面172，液體可經斜面172而流向斜面172 底端的出口 174而回收利用。 本發明之另一態樣係提供一種離心分離方法，此方法 包括：（1)提供一離心分離器190;(2)提供一漏斗承接器15〇 以及一容置桶160，其中該漏斗承接器15〇置於該容置桶 16〇上；以及(3)將漏斗承接器150以及容置桶16〇設置於 201111026 離心分離器l9n e i 之上緣152與中t連接器140下方，且該漏斗承接器 公分至約8〇1八工連接器之下緣142的垂直間距d為約5 動裝置ιι〇、=:如第1圖所示’離心分離器190包括驅 J： 轉桶120、刮刀I30以及中空連接器140。The bucket receiving == giant d can facilitate the handling of the receiving bucket 160. If the distance d between the upper edge 152 and the lower edge 142 of the hollow connector 140 or the spacing d is too small (for example, less than about 5 cm), when the device moves the receiving container 16 and the funnel receiver 15 It is possible that (4) the connector or the receiving bucket 16G) collides or conflicts with the hollow connector 14G or the nearby connector, resulting in (4) the device body or the receiving tub (10). However, if the spacing d is too large (for example, greater than about 8 cm), use a scraper. When the deposit is scraped off, the scraped deposit may splash out of the range that the funnel receiver 150 can take to cause contamination. In addition, the funnel receiver yo should not be directly fixedly attached below the hollow connector 14〇. Because in some applications, the scraped deposits are adhesive and will harden in the air and stick to the funnel to support the H 15〇 surface. If the funnel receiver 15 is directly fixed below the hollow connector 140, the funnel receiver 150 may be clogged due to difficulty in cleaning. In another embodiment, the centrifugal separation system 100 further includes a hollow vessel 170, and the rotating drum 12 is clamped within the hollow vessel 170. When the rotating tub 12 is subjected to the separating process, the separated liquid is separated from the rotating tub 120 via the gap h, and can be collected in the hollow container 170. The bottom of the hollow container 17 can have a slope 172 through which liquid can flow to the outlet 174 at the bottom end of the ramp 172 for recycling. Another aspect of the present invention provides a centrifugal separation method, the method comprising: (1) providing a centrifugal separator 190; (2) providing a funnel receiver 15A and a receiving barrel 160, wherein the funnel receiver 15〇 is placed on the receiving barrel 16〇; and (3) the funnel receiver 150 and the receiving barrel 16〇 are disposed under the 201111026 centrifugal separator l9n ei upper edge 152 and the middle t connector 140, and the funnel The vertical spacing d of the adapter centimeter to the lower edge 142 of the connector is about 5. The device ιι〇, =: as shown in Fig. 1 'The centrifugal separator 190 includes the drive J: the rotary barrel 120, the scraper I30 and hollow connector 140.
置能夠具f中心轴〇:及底部開口 m，驅動裝 130配W Ϊ動轉桶120以中心軸〇為中心旋轉。刮刀 穑你哲旋轉桶12〇内，用以刮除旋轉桶12〇内側的沈 桶120門^空連接器140位於旋轉桶12〇 Τ方，且與旋轉 物質。h’ Γ以林㈣刀i3G刮除的沈積 容置桶16〇T沈 可經由漏斗承接器150而掉落在 雖然本發明已以實施方式揭露 疋本發明，任何熟習此技藝者，，如上’然其並非用以限 範圍内，當可作各種之更動與=不脫離本發明之精神和 圍當視後附之申請專利範圍所界定者=此本發明之保護範 【圖式簡單說明】 為讓本發明之上述和其他目 t 能更明顯易懂，所附圖式之說明如下4寺徵、優點與實施例 第1圖係繪示本發明〜實施 面示意圖。 式之離心分離系統的剖 第2圖係繪示本發明一實施 混合物中固體與液體的剖面示意圖式之旋轉桶120分雜 主要元件符號說明】 12 201111026 離心分離系統 驅動裝置 轉軸 旋轉桶 底部開口 圓柱側壁 傾斜壁 沈積物 刮刀 連桿 轉動機構 中空連接器 下緣 下開孔 漏斗承接器 上緣 上開孔 下開孔 容置桶 環形凸緣 中空容器 斜面 出口 201111026 180進料管 190離心分離器 Ο中心車由 d間距 h間隙 0角度The device can have a f-center axis 〇: and a bottom opening m, and the driving device 130 is equipped with a W-rotating drum 120 to rotate around the central axis 〇. Scraper 穑 哲 哲 哲 旋转 旋转 旋转 旋转 旋转 旋转 旋转 旋转 旋转 旋转 旋转 旋转 旋转 旋转 旋转 旋转 旋转 旋转 旋转 旋转 旋转 旋转 旋转 旋转 旋转 旋转 旋转 旋转 旋转 旋转 旋转 旋转 旋转 旋转 旋转 旋转 旋转 旋转 旋转 旋转 旋转h' 沉积 ( ( 四 四 i 3 3 3 i i i i i i i i i i i i i 沉 沉 沉积 沉 沉积 沉积 沉积 沉积 沉积 沉积 沉积 沉积 沉积 沉积 沉积 沉积 沉积 沉积 沉积 沉积 沉积 沉积 沉积 沉积 沉积 沉积 沉积 沉积 沉积 沉积 沉积 虽然 虽然 沉积 虽然 虽然However, it is not intended to be limiting, and various modifications and changes may be made without departing from the spirit of the invention and the scope of the appended claims. The above and other objects of the present invention can be more clearly understood. The description of the drawings is as follows. FIG. 4 is a schematic view of the present invention. Section 2 of the centrifugal separation system of the present invention is a cross-sectional view of a solid and liquid in a mixture of the present invention. The rotary drum 120 is divided into main components and symbols. 12 201111026 Centrifugal separation system drive unit rotating shaft bottom opening cylindrical Side wall inclined wall deposit scraper connecting rod rotating mechanism hollow connector lower edge lower opening funnel receiver upper edge upper opening lower opening receiving barrel annular flange hollow container inclined surface outlet 201111026 180 feeding tube 190 centrifugal separator Ο center Car by d spacing h gap 0 angle
Di，D〇, Vp 箭頭Di,D〇, Vp arrow