TWI305748B - Device for devision of a non-newtonian liquid flowing through a passage - Google Patents

Device for devision of a non-newtonian liquid flowing through a passage Download PDF

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Publication number
TWI305748B
TWI305748B TW95108011A TW95108011A TWI305748B TW I305748 B TWI305748 B TW I305748B TW 95108011 A TW95108011 A TW 95108011A TW 95108011 A TW95108011 A TW 95108011A TW I305748 B TWI305748 B TW I305748B
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Taiwan
Prior art keywords
plunger
passage
doc
partition
fluid
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TW95108011A
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Chinese (zh)
Inventor
Michael Goinski
Original Assignee
Incoe Corp
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Priority to TW95108011A priority Critical patent/TWI305748B/en
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Publication of TWI305748B publication Critical patent/TWI305748B/en

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Description

1305748 九、發明說明: 【發明所屬之技術領域】 本發明係關於一種用於目標分 流體之裝置。 抓經一通路之非牛_ 【先前技術】 在射出成型中’熔融合成材 如)一复中在茸此忐 π,‘、,、塑材料)穿過(例 ,、干在某些點處存在多 其中在_個通 熱通路歧管系統, 幻通路内供應之炼融好粗—I, 分離成多個分支。此等八^ 兩個排放通路之間被 ._ 叉此荨/刀支主要呈τ形構形。 非牛頓流體流經一圓形 ^ 被細分成多個想像同心空心 、形下’由於該流體 -拋物線流速分佈,且该通:;形此形成該流體之 -流體+ B 4⑽巾^之流速料大。於此 中,忒〜體之數個想像空 大,致相等。 二u圓柱形層之間的切變係 同—非牛頓流體(例如,(熱)流體塑膝)具有不 圓形二Γ情形中,黏度取決於切變,而切變在靠近 近A。㈣料H㈣大1此,靠 见。豕圓形通路壁處 分佈類似-㈣之::小。熔體在該截面上之黏度 意味著:在H +抛物線。於-簡化近似視圖中,此 有類似-柱::路之中心區域内’相對黏稠之流動熔體具 而在周邊區:Γ二大致與該徑向位置無關’ 得,更慢。 體因切麦較大而更具液體態,且流動 此行為圖解闡釋於 、圖a-1 C中。圖1 a顯示一非牛頓流體 丨09350.doc 1305748 (例如’-塑膠溶體)所流經之圓形通路。圖lb顯示截面上 之流速分佈「v」’及圖卜顯示切變之分佈。區域「廿」或 多或少對應於前述柱塞。 /若圖1中一所示類型之非牛頓流體流在通路之—矩形(丁 形)分支T1内轉向且被分離成如圖2中所示的兩個單獨流S1 及S2’則該流體之高黏度部分及液體態部分將分佈在該通 路之截面上。該截面上之分佈顯示於圖3心中,其中區 HV表示高黏度流體而剩餘區LV表示低黏度流體。在圖2至 5中所繪製之座標系統中,座標认y位於該圖式之平面内 而座標z垂直於該圖式之平面延伸。目此,該非牛頓流體 之高黏度HV部分將大體上集中在圖2•中戶斤示料段^及几 之下部部分(在該圖式之方向上)内。此係容易看見,因為 自該通路段i之中心區域所供應之黏性液體(炼體)將前進至 該三通之底部5,且僅隨後才偏轉至圖2方向上之左側及右 側(如圖2中箭頭「a」所指示)’而流入通路i之周邊區域内 流動的更液體態流體將在該通路分支的最開始處(如由箭 頭「b」所指示)偏轉。 若圖2中所示通路段2a&2b係極長,則逐漸地,圖知中 所不之自然分佈將被逐漸地重建。然而實際上,該等通路 段係短,以致圖3b及3c中所示之分佈將大致被保持在遠至 一三通中之下一偏轉。 若在通路段2a中流動之流體遭遇三通其縱向軸沿乂方 向延伸)’則圖4中所示之分佈將在排放通路3&及补中建立 其自身。此處之視圖係在所提及排放通路之流動方向上。 109350.doc 1305748 於該等排放通路中,吾人看見黏性與液體態部分之顯著不 相等以及此等部分相對於該等通路中心之顯著不對稱。 圖2中之三通T3具有兩個垂直於該圖式之平面(在z方向 上)延伸之排放通路4a及4b。參見圖2a,該圖顯示圖2之:匕 部分之-俯視圖。在該三通如偏轉後,導致如圖Μα 中所示該流體之黏性與液體態部分之分離。在自圖2中圖 式之平面向上引出之排放通路4b中’建立根據圖&之分 佈’而在進人圖2中圖式平面之通路辦,建立根據圖% 之刀佈。該視圖同樣係由該三通沿該排放通路之流動方 所界定。 ° 於射出成型中,若連接至射出成型工具⑽模)之注射喷 嘴係自其中不同黏度之溶體組分之數量分佈係不相等(例 如’圖4b及4e)及/或其中炼體分佈不再與通路之縱向轴旋 轉對稱(例如,圖3vb及5b)之多個通路供應原料,則此可導 致鑄造射出成型產品中之缺陷。 若吾人假定藉助分佈在一板面積上方之複數個噴嘴來注 射該板,則可能產生以下缺陷。 若來自該板之外部區域中之噴嘴之液體態炫體部分大於 來自該板之内部區域中之喷嘴之液體態㈣之部分,則在 進入熔體之瞬間壓力下’將迫使更多熔體進入注射工具 (注射鑄模)中該板之外部區域而非中間區域”匕意味著將 給該板之外部區域中每單位面積供應較内部區域中每單位 面積為多之材料’其結果係該鑄造板將包括多個波形邊 緣。相反地’若迫使更多液體態熔體進入注射鑄模之内部 1 ()c)3 50.doc 1305748 區域’則在該熔體冷卻後,該内部每單位面積之較大量嫁 體將導致該板之内部區域中形成一凸脹。 右供應5玄喷'之通路段内之溶體部分係非對稱分佈,則 即使麻煩會減少,但亦仍然產生類似之情形。 例如,若一熱通路歧管系統之數個注射噴嘴之每一個皆 注射一杯子,則各噴嘴之間黏性與液體態熔體之不等量分 佈會導致料杯子將具有不㈣厚度之結果n炫體組1305748 IX. Description of the Invention: [Technical Field to Which the Invention Is Ascribed] The present invention relates to an apparatus for a target fluid separation. Non-cows that catch a passage _ [Prior Art] In the injection molding, the 'melted synthetic material, such as 一, 忐 π, ',,, plastic material) passes through (for example, dry at some point) There are many smelters in the _ _ _ _ _ _ _ _ _ _ _ _ _ _ _ _ _ _ _ _ _ _ _ _ _ _ _ _ _ _ _ _ _ _ _ _ _ _ _ _ _ _ Mainly in a τ-shaped configuration. The non-Newtonian fluid flows through a circle ^ is subdivided into a plurality of imaginary concentric hollows, under the shape 'due to the fluid-parabolic velocity distribution, and the passage: the shape of the fluid-fluid+ The flow rate of B 4 (10) towel is large. In this case, several imaginary bodies are empty and equal. The shear between two cylindrical layers is the same as non-Newtonian fluid (for example, (thermal) fluid plastic In the case of a knee with a non-circular shape, the viscosity depends on the shear, and the shear is close to the near A. (4) The material H (four) is larger than this, and the distribution is similar to the - (4):: small. The viscosity of the melt on this section means: in the H + parabola. In the - simplified approximation view, this is similar - column:: in the middle of the road In the heart region, the 'relatively viscous flow melt has a peripheral zone: Γ2 is roughly independent of the radial position', and is slower. The body is larger and more liquid due to the cut wheat, and the flow is illustrated by Figure a-1 C. Figure 1 a shows a circular path through which a non-Newtonian fluid 丨09350.doc 1305748 (eg '-plastic solution) flows. Figure lb shows the flow velocity distribution "v"' on the cross section and Figure b shows the distribution of the shear. The area "廿" corresponds more or less to the aforementioned plunger. / If the non-Newtonian fluid flow of the type shown in Figure 1 is turned in the - rectangular (but) branch T1 of the passage and Separated into two separate streams S1 and S2' as shown in Figure 2, the high viscosity portion and the liquid portion of the fluid will be distributed over the cross section of the passage. The distribution on the cross section is shown in Figure 3, wherein Zone HV represents a high viscosity fluid and residual zone LV represents a low viscosity fluid. In the coordinate system depicted in Figures 2 to 5, the coordinates y are located in the plane of the pattern and the coordinates z extend perpendicular to the plane of the pattern. Therefore, the high viscosity HV portion of the non-Newtonian fluid will be substantially concentrated in Figure 2 • The middle section of the Zhongjijin section and the lower part (in the direction of the figure). This is easy to see because the viscous liquid (refined body) supplied from the central area of the passage section i Advancing to the bottom 5 of the tee, and only then deflecting to the left and right sides of the direction of Figure 2 (as indicated by arrow "a" in Figure 2) and flowing into the peripheral region of the path i The fluid will deflect at the very beginning of the path branch (as indicated by arrow "b"). If the path segments 2a & 2b shown in Figure 2 are extremely long, then gradually, the natural distribution will not It is gradually rebuilt. However, in practice, the passage segments are so short that the distributions shown in Figures 3b and 3c will be substantially maintained as far below the one-way deflection. If the fluid flowing in the passage section 2a encounters a tee whose longitudinal axis extends in the 乂 direction, then the distribution shown in Fig. 4 will establish itself in the discharge passage 3 & The view here is in the direction of flow of the mentioned discharge passage. 109350.doc 1305748 In these discharge paths, we see significant unequalities between the viscous and liquid states and the significant asymmetry of these parts relative to the centers of the channels. The tee T3 of Fig. 2 has two discharge passages 4a and 4b extending perpendicular to the plane of the pattern (in the z direction). Referring to Figure 2a, there is shown a top view of the Fig. 2: top view. After the tee is deflected, it results in the separation of the viscous and liquid state portions of the fluid as shown in Figure Μα. In the discharge passage 4b which is drawn upward from the plane of the drawing in Fig. 2, 'the distribution according to the drawing &' is established, and in the passage of the drawing plane in Fig. 2, the knives according to the figure % are established. This view is also defined by the flow of the tee along the discharge passage. ° In injection molding, if the injection nozzle connected to the injection molding tool (10) mold is not equal in quantity distribution from the solution components of different viscosity (for example, 'Fig. 4b and 4e) and/or where the refining body distribution is not The plurality of vias that are rotationally symmetric with the longitudinal axis of the via (e.g., Figures 3vb and 5b) supply the material, which can result in defects in the cast injection molded product. If we assume that the plate is injected by a plurality of nozzles distributed over a board area, the following defects may occur. If the liquid glare portion from the nozzle in the outer region of the plate is greater than the portion of the liquid state (4) from the nozzle in the inner region of the plate, then under the pressure at the moment of entering the melt, 'will force more melt into the The outer area of the plate in the injection tool (injection mold) rather than the intermediate area means that the material per unit area in the outer area of the plate will be supplied with more material per unit area than the inner area. Will include multiple waveform edges. Conversely 'if more liquid melt is forced into the interior of the injection mold 1 () c) 3 50.doc 1305748 region ' then after the melt is cooled, the internal per unit area is compared A large number of marshallates will cause a bulge in the inner region of the plate. The solution of the solution in the channel section of the right supply 5 is asymmetrical, and even if the trouble is reduced, a similar situation still occurs. If each of the plurality of injection nozzles of a heat path manifold system injects a cup, the unequal distribution of the viscous and liquid melt between the nozzles will result in the cup having a thickness of (4). Result n dazzling group

分之不對稱分佈將導致優先包含液體態炼體之彼杯子側變 :厚於該杯子之對置側,從而導致—凸脹狀杯子,及/或 右黏性炫體進人鑄模,則其不能抵達該鑄模之底部。 【發明内容】 — 月之一目標係開發藉以最小化或盡可 偏轉導致的不同黏度之m ^除因所 '之桃體組为之不對稱及/或不等量 布及/或防止其發生之震置。 為達成此目標,本發明裎 ϋ政M、 t 、一種用於目標分離一流經 通路(1)之非牛頓流體( 一 -實施例。該材料且有在:融5成材料)之裝置之 形通路分支(丁)中沿截1 偏轉及分離該流體流之 路分it m & 降低之黏度。—隔板係定位於土 ⑺將來自供應通路段(― 一適合於在供應隔板⑴)之角度位置較佳具肩 設定值。藉助本㈣/佈該流體之不同黏性組分之 顯分佈之情形下達成遥路未形成不同黏性組分之明 該流體之分離。 刀叉(Ό之排放通路(2a、2b)之間 I09350.doc 1305748 猎助本發明之此實施例,所產生 佳或大體上丁形通路分支之供應通月形係:當處於-較 熔體組分係非旋 x内時,不同黏度之 ρ灰轉對稱分佈。相反, 個排放通路段内, 牧邊專通路分支之兩 等。 …又之熔體組分之比例係大體相 於本發明之—第-奢被点丨士 料流。 , β供—偏轉板以分離該材 於該裝置之此第二形式中,在一 分支之供應通路段内,不同黏度之峰且八-上τ形通路 旋轉對稱。於該通 、、刀之數置分佈係 持㈣對稱分佈且兩個排放通路中不同黏=質^呆 比例亦大體上相等。該排放通路段内之八:、、、’且刀之 供應段内之彼分佈圖形實質上相同。“布圖形因此與該 等排放通路可具有與該供 等排放通路中之、#略相问之截面’以使該 路可且有較小選擇係,該等排放通 【實::二截面,以使流速不急劇降低或根本不降低。 圖6 a及6 b以實你丨太_ 上rr· 貫例方式顯不一在原理上具有根據本發明之 一第—裝置類型之結構之實施例。於該通路分支中一 在:應炫體之隔板U經安裝以使其分離來自供應通路段曰1 /;,L此處,隔板11被置放成此—旋轉角度以致其可 分開正接近之炫體’其中係以該兩個部分流包含相等數量 的不同黏度之流體组分之方式使具有不同黏度之流體纽分 不與该通路之縱向軸旋轉對稱分佈。 I09350.doc 1305748 中之情形下該《自己分佈在與圖6a 角度位置置1」之相隔排放通路之間,則以圖6b中所示 體供應至兩個排同比例之黏性及液體態流 、南古斗 _ 之方式分開正接近之熔體。可以合 、方式將隔板11佈置於 可調角度位置。、通路刀支内,使其具有固定調節或 根據本發明之此一 於圖 、之貫際實施例係以實例方式顯示 談 。於圖W ’自該T形通路分支之底部6開始在 ' ;作"~搪孔12 ’進入該塘孔12 ’將隔板柱塞1〇壓 入非放通路段22a、22b内遠至其中間為止,板 … 裝至^板柱塞ϊ〇β此處,該隔板柱塞係(例 月’萬13被旋轉至合意角度位置中,如圖6,b所 圖解說明。為防止柱塞10在運行壓力下被推出,藉由一螺 奴塞14將其固疋在其軸向位置中’螺旋塞μ可藉由(例如) :六角承窩⑽合至搪孔12内。柱塞職佳係—在其靠近 隔板11之端處具有—圓頂形凹陷16之實心體,纟中隔板^ 係以其側背向供應通路段i之任何方式剛性地固定。隔板 "之必需角度位置係由隔板柱塞10插入搪孔12内之旋轉位 置所決定。該角度位置之保持係以任何習用方式所達成, 例如’藉由一壓配合、或藉由任何其他額外之合適旋轉固 定方式。 方便地,在已將先前所述之柱塞安裝在通路分支内後, 自排放通路22a及22b開始將隔板柱塞10鑽孔至圓頂形凹陷 16之區域内該等排放通路之直徑,從而形成(在投影上): I09350.doc 10 1305748 圓形流動開口 17。當然’亦可在安裝該隔板柱塞之前提供 該等流動開口。 在圖7中,為清晰起見,將隔板丨丨描繪為處於一垂直於 該圖式平面之角度位置中,且將由該搪孔形成之開口 17描 繪為處於該圖式之平面内。將瞭解,實際上,此等流動開 口 17處於旋轉90。狀態,而隔板丨丨之角度位置採取一與該 圖式之平面相關之角度位置,如圖6b中所示,其適合於不 同黏度之流體組分在供應通路1内之分佈。 於圖7中,圖中顯示通路分支之底部6具有一加強件18。 僅在商用一通、或一其中該等流動通路所工作之熱通路 歧管區塊之壁具有-不充分厚之料,方才需要加強件 18 ° 圖8a及8b顯示兩個先前所述具有隔板丨丨之實心隔板柱塞 ίο之實例之透視圖。圖8a顯示在鑽孔圓頂形凹陷16前之柱 塞1〇’其中顯示有後六角承窩13。圖化顯示具有方便地在 安裝後製作之搪孔及所形成之流動開口丨7之柱塞。 /於根據本發明之一裝置之第二實施例中,所追求之目標 係如此在通路分支内分離及偏轉具有根據圖之不同黏 度之流體組分之對稱分佈的—流體流以致大體上在該通路 分支之排放通路内保持該分佈。 右在圖9b中’假定供應通路段21中之流體係根據圖域 分佈’則排放通路段22a及22b中之分佈將大致對應於圖% 及3C。但,假若人們將自上方(該圖式中之方向)且另外亦 自下方’…亥通路分支供應一與管道21所供應之流體流相等 109350.doc 1305748 之流體流,則容易地看到在圖9b中被強迫沿側面進入通路 22a及22b之黏性流體組分將被所設想之額外流體流朝向通 路2 2 a及2 2 b之中心偏移。 此效應係藉由具有一普通通路分支的本發明裝置之第二 類型所達成。於根據本發明之一裝置之第二類型中,在該 供應通路段之中心内流動之黏性流體組分經分離,且該: 個組分各自大體上以直角在該等排放通路段之入口處交 匯,其在此交匯處之流動方向係實質上垂直於該等排放通 路之縱向方向。 =成此目的’在該通路分支中,存在_偏轉板Μ,該 偏轉板23之形狀使得係—刀鋒24進入供應通路仙且實質 上將在通路段2 1之中心内户叙★迷t ω、+ 八/ ^動之黏性流體組分分成兩個組 刀’一個組分繼續在偏轉板23之左側流動而另—组分在偏 :板流動。該等組分經偏轉以使其盡可能在該通 刀支之底知7(該圖式中之方向)處以直角相互交匯。 該黏性組分之兩個組分撞擊在其兩側上之腹板27僅用於 I偏轉板23機械地附裝於該通路分支内。對於本發明之效 二實際偏轉板23較佳不在其整個周邊上 < 1士何地方觸及通路段2 I 〇 連圖轉板23之一實際實施例。該腹板Μ 3】。养助外3]具Γ大直徑之圓柱形段32内之圓柱形段 之搪孔被推至又、/ 轉板穿過一位於該通路分支底部内 圖,所示之位置且被密封緊固。 、 料板23於該通路分支内之任何類型之緊固將 • 12· 1 ()幻 50.doc 1305748 足矣’例如,藉助圖9a中虚線所示之支柱28,雖然此對於 小直徑通路可能係困難。The asymmetric distribution of the fraction will result in the side of the cup containing the liquid state refinement preferentially: thicker than the opposite side of the cup, resulting in a bulging cup, and/or a right viscous glare entering the mold, then Cannot reach the bottom of the mold. SUMMARY OF THE INVENTION - One of the goals of the month is to develop a different viscosity for minimizing or deflecting, to eliminate the asymmetry and/or unequal amount of cloth and/or prevent it from occurring. The shock is set. In order to achieve this goal, the present invention is in the form of a device for separating a first-class passage (1) of a non-Newtonian fluid (a - embodiment. The material is: a material of 50) The path branch (D) intercepts and deflects the fluid flow path by dividing it m & reducing the viscosity. - The partition is positioned in the soil (7) to have a shoulder setting from the supply passage section ("one suitable for the supply partition (1)). By means of the (4)/clothing distribution of different viscous components of the fluid, the separation of the fluid is achieved without the formation of different viscous components in the remote path. Knife and fork (between the venting passages (2a, 2b) I09350.doc 1305748 Hunting for this embodiment of the invention, the supply of the good or substantially butyl-shaped branch branches is provided by the moon-shaped system: when in-melt When the components are not in the x-rotation, the ρ of the different viscosities are symmetrically distributed. Conversely, in the discharge passage section, the grazing-side special passage branches are two. The ratio of the melt components is generally in the present invention. - the first - extravagant point is the gentleman stream. , β supply - deflection plate to separate the material in the second form of the device, in a branch of the supply passage segment, the peak of different viscosity and eight - up τ The shape of the passage is rotationally symmetrical. The distribution of the number of the passages and the knives is symmetrically distributed (4) and the ratios of the different viscosities and masses in the two discharge passages are substantially equal. The eight in the discharge passage section: , , , And the distribution pattern in the supply section of the knife is substantially the same. "The cloth pattern and thus the discharge passages may have a cross section with the # in the supply passage, so that the road can be smaller. Selection system, these emissions pass [real:: two sections, so that the flow rate is not urgent Reducing or not reducing at all. Figures 6a and 6b show an example of a structure of a device type according to one of the present inventions in a conventional manner. In the first one, the partition U of the glare should be installed to separate it from the supply passage section 曰1 /;, where the partition 11 is placed so that the angle of rotation is such that it can be separated from the glare 'In the case where the two partial streams contain an equal number of fluid components of different viscosities, the fluid kinks having different viscosities are not rotationally symmetrically distributed with the longitudinal axis of the passage. I09350.doc 1305748 in the case of It is distributed between the discharge passages which are set to 1" at the angular position of Fig. 6a, and is directly adjacent to the two viscous and liquid flow streams in the same proportion as shown in Fig. 6b. Melt. The partition 11 can be arranged in an adjustable angular position, in the passage knife, so that it has a fixed adjustment or according to the present invention, the embodiment is shown by way of example. Talk. Figure W' from the T-shaped path The bottom 6 of the branch begins at ';&&;~搪孔12' enters the pond hole 12' and presses the spacer plunger 1 into the non-displacement section 22a, 22b as far as it is, the board... Plate plunger ϊ〇 β Here, the diaphragm plunger system (in the case of the month '10,000 is rotated to the desired angular position, as illustrated in Figure 6, b. To prevent the plunger 10 from being pushed out under operating pressure, The screw plug μ is fixed in its axial position by a screw plug 14 by, for example, a hexagonal socket (10) that fits into the bore 12. The plunger is in the vicinity of the partition At the end of the elbow, there is a solid body of a dome-shaped recess 16 which is rigidly fixed in any manner with its side back facing the supply passage section i. The necessary angular position of the partition is defined by the partition column The position of rotation of the plug 10 into the bore 12 is determined. The retention of the angular position is achieved in any conventional manner, such as by a press fit, or by any other additional suitable rotational fixation. Conveniently, after the previously described plunger has been installed in the passage branch, the diameter of the discharge passages in the region of the dome-shaped recess 16 is drilled from the discharge passages 22a and 22b, Thereby formed (on the projection): I09350.doc 10 1305748 Circular flow opening 17. Of course, these flow openings can also be provided prior to installation of the bulkhead plunger. In Fig. 7, for clarity, the spacer 丨丨 is depicted as being in an angular position perpendicular to the plane of the pattern, and the opening 17 formed by the pupil is depicted as being in the plane of the pattern. It will be appreciated that, in effect, such flow openings 17 are at a rotation of 90. The state, and the angular position of the spacer 采取 takes an angular position associated with the plane of the pattern, as shown in Figure 6b, which is suitable for distribution of fluid components of different viscosities within the supply passage 1. In Figure 7, the bottom portion 6 of the passage branch is shown with a stiffener 18. Reinforcement 18 ° is required only in the case of a commercial pass, or a wall of a heat path manifold block in which the flow paths operate - an insufficiently thick material. Figures 8a and 8b show two previously described partitions. A perspective view of an example of a solid partition plunger ίο. Figure 8a shows the plunger 1' in front of the bored dome-shaped recess 16 in which the rear hexagon socket 13 is shown. The figure shows a plunger having a bore which is conveniently fabricated after installation and a flow opening 7 formed. / In a second embodiment of the device according to the invention, the object sought is to separate and deflect a fluid flow having a symmetrical distribution of fluid components according to different viscosities in the path branch so that substantially This distribution is maintained within the discharge path of the branch branch. Right in Fig. 9b 'Assume that the flow system in the supply passage section 21 is distributed according to the map domain', the distribution in the discharge passage sections 22a and 22b will roughly correspond to the graphs % and 3C. However, if one would supply a fluid flow equal to the fluid flow supplied by the pipe 21 from the lower (in the direction of the drawing) and from the lower '...Hai passage branch, 109350.doc 1305748, it is easy to see The viscous fluid component forced into the passages 22a and 22b along the sides in Figure 9b will be offset by the envisaged additional fluid flow towards the center of the passages 2 2 a and 2 2 b. This effect is achieved by the second type of device of the invention having a common path branch. In a second type of apparatus according to the invention, the viscous fluid component flowing in the center of the supply passage section is separated and the: each component is substantially at right angles to the inlet of the discharge passage section At the intersection, the flow direction at the intersection is substantially perpendicular to the longitudinal direction of the discharge passages. = for this purpose 'in the path branch, there is a deflection plate Μ, the shape of the deflection plate 23 is such that the system-blade 24 enters the supply path and will substantially be in the center of the channel segment 2 1 The +8/^ moving viscous fluid component is divided into two sets of knives 'one component continues to flow on the left side of the deflector plate 23 and the other component in the bias: plate flow. The components are deflected such that they intersect each other at right angles at the bottom of the blade (in the direction of the drawing). The web 27 on which the two components of the viscous component impinge on both sides is only used for mechanical attachment of the deflector 23 to the passage branch. For the effect of the present invention, the actual deflector plate 23 preferably does not have an actual embodiment of the entire area of the passage section 2 I 〇 connected to the turn plate 23. The web Μ 3]. 3) The bore of the cylindrical section in the cylindrical section 32 having a large diameter is pushed to the end, and the flap is passed through a position in the bottom of the branch of the passage, shown and sealed. . Any type of fastening of the web 23 within the branch of the passage will be 12.doc 1305748 sufficient, for example, by means of the strut 28 shown in phantom in Figure 9a, although this is for small diameter passages. It may be difficult.

可將具有腹板27及圓柱形段3 1之偏轉板23製作在連續圓 柱形體之外,在其前端設置刀鋒24及在其後端設置一縮 頸’該縮頸藉由彼此相對且平行於刀鋒24之兩側上之缺口 形成腹板27。該偏轉板之對置側25較佳位於圓形或類似彎 曲表面上’該等表面自刀鋒24延伸至腹板27且形成一進入 原圓柱體3 1之表面之過渡段。 圖11顯不一安裝在一 T形通路分支内的圖11之類型之偏 轉板在圖11中之參考編號對應於圖9及10中之彼等參考 編號之情形下,該等參考編號表示與彼等圖式中相同之物 件。 當結合附圖時,自以下說明中將獲知本發明之其他細 卽、益處及特徵。 【圖式簡單說明】 在上文中,已以實例方式依據實施例及依據附加圖式圖 解闡釋了本發明,在圖式中: 圖la-lc顯示一非牛頓流體在一圓柱形通路中之流動情 形。 圖2顯示一具有三個丁形通路分支之通路歧管系統, 圖2a以俯視圖形式顯示圖2之一部分。 圖3a-3c顯示在一笫__規增八± w 弟通道刀支T1後面的該等黏性及 體恶流體組分最初對稱分佈之分佈, 圖4a 4c顯示自該第一通路分支τι繼靖、 刀又11、-疆續流動之炫體遭沒 109350.doc 13 1305748 一與先則所通過之通路分支T1處於相同平面内之通路分支 T2之分佈, 圖5a-5c顯示在一處於一垂直於先前所通過之通路分支 T1之平面内之後續通路分支T3處的與圖4中對應之分佈, 圖6a及6b以實例方式圖解闡釋本發明之一第一實施例, 該第-實施例在原理上具有一第一裝置形式之結構。The deflector plate 23 having the web 27 and the cylindrical section 31 can be formed outside the continuous cylindrical body, with a blade 24 at its front end and a constricted neck at its rear end. The necks are opposite and parallel to each other. The notches on both sides of the blade 24 form a web 27. The opposite side 25 of the deflector plate is preferably located on a circular or similar curved surface' which extends from the blade 24 to the web 27 and forms a transition into the surface of the original cylinder 31. Figure 11 shows a deflection plate of the type shown in Figure 11 mounted in a T-shaped branch branch. The reference numbers in Figure 11 correspond to the reference numerals in Figures 9 and 10, and the reference numbers indicate The same objects in their drawings. Other details, advantages and features of the present invention will become apparent from the description and appended claims. BRIEF DESCRIPTION OF THE DRAWINGS In the above, the invention has been illustrated by way of example and with reference to the accompanying drawings, in which: Figure la-lc shows the flow of a non-Newtonian fluid in a cylindrical passage situation. Figure 2 shows a via manifold system having three butt-shaped branch branches, and Figure 2a shows a portion of Figure 2 in a top view. Figures 3a-3c show the distribution of the initial symmetric distribution of the viscous and body fluid components behind a 笫 _ _ _ _ _ _ _ _ _ _ _ _ _ _ _ _ _ _ _ _ _ _ _ _ _ _ _ _ _ _ _ _ Jing, Knife 11 and the continuation of the continuation of the movement of the genre 109350.doc 13 1305748 The distribution of the branch branch T2 in the same plane through the path branch T1 passed by the first, Figure 5a-5c shows in one A first embodiment of the present invention is illustrated by way of example, with respect to a distribution corresponding to that in FIG. 4 at a subsequent path branch T3 in the plane of the previously passed path branch T1, which is illustrated by way of example, the first embodiment In principle, it has a structure in the form of a first device.

圖7顯示一根據圖6的一裝置之第一類型實施例之實際實 例,其構建於一T形通路分支内。 圖8a及8b在各自圖式中顯示圖7中所用分離柱塞之一實 施例之實際實例, 、 圖9a及9b在各自圖式中顯 類型實施例之一實際實例, 路分支内之兩個區段中, 示根據本發明之一震置之第二 其彼此成直角構建於一 T形通 圖以兩個彼此成直角之視圖以—放… 圖a及9b中所㈣轉板之—實施例之實際Figure 7 shows a practical example of a first type of embodiment of a device according to Figure 6, constructed in a T-shaped path branch. Figures 8a and 8b show, in respective figures, a practical example of one embodiment of the separating plunger used in Figure 7, and Figures 9a and 9b are practical examples of one of the embodiments of the type in the respective figures, two of the road branches In the section, the second according to one of the present inventions is constructed at right angles to each other and is constructed at a right angle to a T-shaped view at two right angles to each other to be placed in (a) the transfer plate of Figures a and 9b. Practical example

一繁固部件。 甲戈曰刀 1 通路(供應通路段) 2a 排放通路 2b 排放通路 3a 排放通路 3b 排放通路 4a 排放通路 109350.doc 1305748A sturdy component.曰戈曰刀 1 passage (supply passage section) 2a discharge passage 2b discharge passage 3a discharge passage 3b discharge passage 4a discharge passage 109350.doc 1305748

4b 排放通路 6 底部 7 底端 10 隔板柱塞 11 隔板 12 搪孔 13 六角承窩 14 螺旋塞 15 六角承窩 16 圓頂形凹陷 17 流動開口 18 加強件 21 通路(供應通路段 22a 排放通路 22b 排放通路 23 偏轉板 24 刀鋒 25 側 27 腹板 28 支柱 31 圓柱形段 32 圓柱形段 a 箭頭 b 箭頭 管道) 109350.doc -15- 13057484b Discharge path 6 Bottom 7 Bottom end 10 Separator plunger 11 Separator 12 Boring 13 Hex socket 14 Screw plug 15 Hex socket 16 Dome recess 17 Flow opening 18 Reinforcement 21 Path (supply passage section 22a discharge path 22b Discharge path 23 Deflection plate 24 Blade 25 Side 27 Web 28 Pillar 31 Cylindrical section 32 Cylindrical section a Arrow b Arrow pipe) 109350.doc -15- 1305748

d 51 52 T T1 T2 丁 3 區域 單獨流 單獨流 T形通路分支 線 通路分支(通道分支) 通路分支(三通) 通路分支(三通)d 51 52 T T1 T2 D 3 zone separate flow separate flow T-shaped branch branch line branch branch (channel branch) path branch (three-way) path branch (three-way)

I09350.doc -16-I09350.doc -16-

Claims (1)

130没號專利申請案 中文申請專利範圍替換本(9、7年5月) 十、申請專利範圍·· 1 ·種用於分離流經一通路(1)之非牛頓流體材料之裝置, 材料具有一在流經一偏轉及分離該流體流之大體上T 、路刀支(丁)時沿截面向外降低之流動調節黏度,該裝 括8比姊該通路分支(丁)内供應通路之末端定位的隔 板(11),該隔板(11)將來自該供應通路段(1)之逆向流動 :IL體刀離成兩纟’該隔板(11)之角度位置具有一適於在 該供應通路段(1)内分佈該流體之不同黏性組分之設定 值’其中流入該等排放通路内之該流體大體上不具有該 流體之該等不同黏性組分之分佈。 2. 如响求項1之裝置,其中該隔板⑴)在其角度位置上係可 調整。 3. 如凊求項1之裝置,其中該隔板⑴)係藉助一隔板柱塞 (二〇)定位於該通路分支⑺内,該隔板(11)係藉助該通路 刀支(T)内一搪孔(12)附裝至該隔板柱塞(10)。 _ 4.如睛求項2之裝置,纟中該隔板(11)係藉助一隔板柱塞 (二〇)定位於該通路分支⑺内,該隔板(u)係藉助該通路 刀支(Τ)内一搪孔(12)附裝至該隔板柱塞(10)。 5. 如明求項3之裝置,其中位於一田比鄰該供應通路段⑴之 第一端處之該隔板柱塞(1〇)具有一其中緊固有該隔板⑴) 之圓頂形凹陷(16)。 6. 如》月求項5之裝置,#中該圓頂形凹陷(16)被沿該等排放 通路(2a、2b)之方向鑽開。 7. 如凊求項3之裝置,其中為固定該隔板柱塞⑽之縱向位 109350-970516.doc 1305748 置,可將一螺旋塞(14)旋入該隔板柱塞背面之該搪孔 (12)内。 8.如請求項4之裝置,其中為固定該隔板柱塞(10)之縱向位 置,可將一螺旋塞(14)旋入該隔板柱塞背面之該搪孔 (12)内。130 No. Patent Application Chinese Patent Application Substitute Replacement (June, May, 2017) X. Patent Application Range · · · A device for separating non-Newtonian fluid materials flowing through a passage (1) a flow-adjusting viscosity that decreases outwardly along a section when deflecting and separating a substantially T-way blade of the fluid stream, the inclusion of 8 the end of the supply passage in the branch (D) a positioning partition (11), the partition (11) will reverse flow from the supply passage section (1): the IL body knife is separated into two 纟 'the angular position of the partition (11) has a suitable A set value for the distribution of different viscous components of the fluid within the supply passage section (1) wherein the fluid flowing into the discharge passages has substantially no distribution of the different viscous components of the fluid. 2. The device of claim 1, wherein the partition (1) is adjustable in its angular position. 3. The device of claim 1, wherein the partition (1) is positioned in the passage branch (7) by means of a bulkhead plunger (11) by means of the passage knife (T) An inner bore (12) is attached to the bulkhead plunger (10). 4. The apparatus of claim 2, wherein the partition (11) is positioned in the passage branch (7) by means of a bulkhead plunger (u) by means of the passage knife (Τ) A bore (12) is attached to the bulkhead plunger (10). 5. The apparatus of claim 3, wherein the spacer plunger (1〇) located at a first end of the supply passage section (1) is a dome-shaped recess in which the partition (1) is fastened. (16). 6. In the apparatus of the month 5, the dome-shaped recess (16) is drilled in the direction of the discharge passages (2a, 2b). 7. The device of claim 3, wherein a screw plug (14) is screwed into the bore of the back of the diaphragm plunger for fixing the longitudinal position 109350-970516.doc 1305748 of the spacer plunger (10) (12) inside. 8. The device of claim 4, wherein to secure the longitudinal position of the spacer plunger (10), a screw plug (14) can be threaded into the bore (12) of the back of the spacer plunger. 109350-970516.doc Ϊ305^^8ι〇8011號專利申請案 中文圖式替換本(97年5月) 十一、圖式: Scherung109350-970516.doc Ϊ305^^8ι〇8011 Patent Application Chinese Graphic Replacement (May 97) XI. Schema: Scherung 圖la 圖lb 圖ic yFigure la Figure lb Figure ic y 109350-970516.doc Ϊ305748109350-970516.doc Ϊ305748 109350-970516.doc •2 Ϊ305748109350-970516.doc •2 Ϊ305748 109350-970516.doc 1305748109350-970516.doc 1305748 109350-970516.doc 4 1305748109350-970516.doc 4 1305748 圖11 109350-970516.docFigure 11 109350-970516.doc
TW95108011A 2006-03-09 2006-03-09 Device for devision of a non-newtonian liquid flowing through a passage TWI305748B (en)

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