TW201226309A - Micro-pump - Google Patents

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TW201226309A
TW201226309A TW99147390A TW99147390A TW201226309A TW 201226309 A TW201226309 A TW 201226309A TW 99147390 A TW99147390 A TW 99147390A TW 99147390 A TW99147390 A TW 99147390A TW 201226309 A TW201226309 A TW 201226309A
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fluid
development zone
section
vibrating
outflow
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TW99147390A
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Chinese (zh)
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TWI448414B (en
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An-Bang Wang
Ming-Che Hsieh
Wen-Hui Tsai
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Univ Nat Taiwan
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Abstract

The present invention relates to a micro-pump for conveying a work fluid comprising: a vibrating chamber for containing the work fluid; an inlet and an outlet respectively communicated with the vibrating chamber for providing the work fluid entering the vibrating chamber via the inlet and flowing out of the vibrating chamber via the outlet; and a first flow pattern developing region having a flow pattern developing space for the work fluid to develop its flow pattern, where the vibrating chamber is communicated with the inlet and the outlet via the first flow pattern developing region.

Description

201226309 六、發明說明: 【發明所屬之技術領域】 本發明係指-種無賦微型幫浦,尤其是—纖械賊無閱式微 【先前技術】 目現有技術之巾微幫舰種類«,主要可概分為麵式與非機 械式兩種。機械式微幫義最大優點^受特殊紅作流體限制,其 依致動器賴___各有設計;麵械式幫獻致上則受其工 作流體之性質舰制,像是電泳、電滲透式等只_於帶有電荷或且 極性分子的X作缝,這碰f浦流賴低,通常需錄大的工作電 壓’其他如氣泡式、磁性越動力式等的微幫浦,也各有其應用上的 限制。 在機械式微幫浦中又以薄膜位移式(簡稱薄膜式)占其中的大多 數’為目前研究的主流之倘針對微幫浦的致航件與閥門進行文 獻整理暨專利檢索,可發現「壓電式」係為目絲多種類的致動器中 產學研究顧之域,倘依_種類,壓電式微幫浦可分為「有間式」 與「無閥式」兩大類,其忖赋又可分為具有絲_具有被動闊 兩種,被_在近鱗已騎邁人成»,所投从輕研究力已趨 向f°,無閥式的專利統計件數雖少於其他閥Η種類,但由於其結構 簡: ' 無=件及不需耗能且無、阻塞等問題,近年來已成為學界 研究之主流’顯示無閥式微幫浦仍處於萌芽開發期,擁有很高的發展 性與發明的空間。 最早由Stemme等人,在美國專利第US62〇329i號中提出之擴散 器/嘴嘴幾何構型的無閥式幫浦,年涂等人(涂智凯,「新式無閥門 201226309 微幫浦之開發」,台灣大學應用力學研究所碩士論文2004)也提出一擋 體式之無閥式微幫浦設計,2〇〇5年新加坡的Ng等人,在美國專利第 US691〇869號中提出利用機翼形狀(airfoil)之擋體來進行幫浦流道設 計,而在 2006 年 Izzo 等人(Ivano l2zo, Dino Accoto, Arianna Menciassi, Lothar Schmitt, Paolo Dario, <{Modeling and experimental validation of a piezoelectric micropump with novel no-moving-part valves^, Sensors and Actuators A-Physical,Vol.l33: 128-140,2007)改變擴散器 /喷嘴的幾何構 型’讓流體指向性能夠再有所提高,同年韓國的Y〇on等人(jae Sung Yoon, Jong Won Choi, II Hwan Lee, Min Soo Kim, eiA valveless micropump for bidirectional applications”,Sensors and Actuators A-Physical,Vol. 135: 833-838, 2〇07)提出另一創新無閥式之設計,並提出此一幫浦具有雙方 向之流動性,由上述文獻可確知,無閥式幫浦之研究是目前極為熱門 的主題。 目前無閥式微幫浦主要可分為以下四類: (1) 喷嘴/擴散器:利用漸擴有較小流阻(正向)、漸縮有較大流阻 (反向)之差異性,而有淨流量,約占無閥式微幫浦設計的6〇%,為目 前主要之無閥式研究主題。 (2) 主、侧支流道:此類型設計皆是利用主、側支流道之流阻差 異性來其功心例如:騎拉P邮献由_魏㈣驗道所構成, 直線流道正向流阻較小’而姻料流道來増加励雜,以造成正 反向之差異性,約占無閥式微幫浦設計的15%,如美國專利第 US5876187號所揭露。另外,在·6年γ〇〇η所提出的在直線流道加 上-側支流道連接振動腔,來達成不對稱結構之設計;其並f試反向 串聯兩個微幫浦’以達雙向輸送流體之目的。 201226309 (3) 擋體式:在直線流道内加人(_、機翼職體),其為喷 嘴/擴散it之延伸變形設計,約占無閥式微幫浦設計的5%。 (4) 血管流式:在哺乳動物_胎_,續尚未發育形成,血 液在血管巾驗動方式亦是無戦的概念之―,即在流道結構不對稱 點處為往《朗施力點喊雜量產邮如___,約占 無閥式微幫浦設計的15%。 %綜觀上述的各種無閥式微幫浦的研究皆著重在整流器㈣㈣的 設計及最佳化,而其他部位元件的影_卩鮮少被加財量及探討,此 原因為無贼微_作動的顧是整流器 合一週紐㈣之壓力較«相錢往«财^淨^ 量,而達流體傳輸之目的;所以在過往無閥式微幫浦的研究中,皆單 純以壓力的角度來看待其他部份元件,如振動賴的功用只被視為提 供整流器有-壓力源賴化,且流體•、出口也只單純被考量為與 外界連通之介面而已。 鳩年Higashi等人,在美國專利第仍顺請號中曾提出一 新式的無閥驅動概念’其整流器之設計方式為在振動腔體兩側分別接 上-短-長之不對稱流道’接著利用一非對稱工作周期(即一 _ 不等於5〇/。)之壓力變化源來達到流迦動,制在紐專利中提出一 緩衝區(壓力吸收_設計概念可改善流體傳輸的鱗,但其出發點 仍與過往㈣式普遍轉力鱗量社場_,並未真正考慮整流器 以外其他部分元件流場變化所帶來之影響。 2〇〇9年由王等人(謝明哲,「無閥式微幫浦之腔體設計與作動機制 研究」’台灣大學細力學研究所碩士論文2_)提出—新型微幫浦腔 體設計,其發現無狀微幫_振__存在著麟狀流場,而 此-雕流場之發展與微幫浦之效能有著顯著且高度相關之特性,盆 201226309 根據此-渦漩發展在振動腔體内加人導流元件,期使微㈣效率獲^ 明顯提升。 于 有鑑於此,申請人,經過悉心試驗與研究,並一本鐵而不捨 神’終構思出本案「微鄕浦」,關克服上述缺點,町為本 簡要說明。 ' 【發明内容】 本發明係在流體入(出)口與整流器之間加入一適當大小與數目的 「流態發展區」’在流態發展區中,人口難/麟與出,旋/渦流 可充分發展,同時可降低人σ處與出σ處的颇,因缸作流體可以 很容易的流入進流口,也可以很容易的排出出流口,故可使得幫浦的 流體傳輸效率獲得大幅之改善並增加輸送流量 流態發展區可進-步的被設計與被變化為各種不同的尺寸、大 小、雜敝合,_整微幫浦的工作曲線,使本發_微型幫浦具 有更多元而廣泛的應用。 因此根據本發明的第-構想,提出一種微型幫浦,用以輸送一工 作流體,其包括:一振動腔室,用以容納且驅動該工作流體;一進流 口與一出流口,其分別與該振動腔室相連通,供該工作流體經由該進 流口流入該振動腔室並經由該出流口流出該振動腔室;以及一第一流 態發展區,其具有一流態發展空間供該工作流體發展其流態,該振動 腔室係經由該第一流態發展區與該進流口或者該出流口相連通。 因此根據本發明的第二構想,提出—種微幫浦,用以輸送〆流 體,其包括:一進口與一出口; 一流態發展區,其具有一流動發展空 間供該流體發展其流態;一振動腔體,其經由該流態發展區與該進口 或者該出口相連通並容納且驅動該流體。 201226309 【實施方式】. 本案將可由以下的實施例說明而得到充分瞭解,使得熟習本技藝 之人士可以據以元成之,然本案之實施並非可由下列實施案例而被限 制其實施型態。 第一實施例 請參閱第1A圖及第1B圖,其揭示的微幫浦1〇〇主要包括振動腔 室110、進流口 120、出流口 130、進流段整流器14〇、出流段整流器 150、振動薄膜160、致動器170、進流段流態發展區18〇及出流段流 態發展區190。 進流口 120是連通於進流段流態發展區18〇,其用以銜接外部輸 送管路’以垂直(vertical)或水平(horizontal)的方式導入流體;出流口 13〇 是連通於出流段流態發展區190,其用以銜接外部輸送管路,可以垂 直或水平的方式導出流體。 如第1B圖所示,振動薄膜16〇是設置於振動腔室11〇之上;致動 器Π0則連接於振動薄膜1(30,其用於振動薄膜16〇進行往復振動, 致動器170較佳地可以是壓電元件、電磁驅動元件、熱驅動元件、氣 動薄膜元件、機械振動元件或熱氣驅動元件;舉例來說,當致動器17〇 為壓電元件時,藉由壓電元件之往復伸縮,即可使得振動薄膜16〇產 生往復擴張與擠壓之變形,進而達成振動薄膜16〇產生往復運動 (m:iprocatingmotion)之效果,從而使振動腔室11〇内的流體產生運動。 如前所述,當致動器Π0驅使振動薄膜16〇進行往復運動時,振 動腔室110之内部空間或體積即可產生往復的增大與縮小。更詳細的 說,當振動薄膜160向上運動(吸入模式)時,振動腔室11〇内之壓力會 低於外界壓力而產生負壓狀態,因而使得流體經由進流口 12〇、進流 201226309 段流態發展區180、出流段流態發展區19〇和出流口 130被吸入至振 動腔室110之中;反之,當振動薄膜160向下運動(排出模式)時,振動 腔室110内之壓力會高於外界壓力’因而使得流體經由進流口 120、 進流段流態發展區180、出流段流態發展區190和出流口 130流出振 動腔室110。 進流段整流器140是連接於振動腔室110與進流段流態發展區18〇 之間,其用以匯整並緩衝於進流段流態發展區180及振動腔室no間 往復來回流動之流體;出流段整流器150是連接於振動腔室ι1〇與出 又biL態發展區190之間’其用以匯整並緩衝於振動腔室11〇及出流 段流態發展區190間往復來回流動之流體;進流段整流器和出流段整 流器經由改變其幾何形狀設計,而使得流阻具有方向性,以提升薄膜 式微幫浦之運作效能。進流段整流器M0與出流段整流器15〇係作為 連通元件,進流口 120與出流口 130可分別經由兩個連通元件與振動 腔室110相連通。 更具體而言,進流段整流器M0具有從進_流態發展區18〇往 振動腔室110逐漸擴大之形狀,而出流段整流器15〇具有從振動腔室 110在進流段流態發展H携逐漸擴大之形狀。當振動薄膜娜向上 運動(吸入模式)時,對於流體經由進流段整流器⑽才目較於經由出流 段整流器150至振動腔g 11〇之流動而言,其流阻較小;反之,當振 動薄膜_向下運動(排出模式)時,對於流體由振動腔室ιι〇經由出流 段整流器150相較於經由進流段整流器14〇之流動而言,其流阻較小, 因而達到細式微幫浦之運作效能。本實施例之職段整流器及 出流段整流ϋ亦可峨时嘴、御^、躺拉贼其絲何可達成 流阻具有差異性之結構及處理(如表硫疏水處理)。 進流段流態發展區180是連通於進流段整流器U0和進流口 120 201226309 之間,其可緩衝流入和流出振動腔室110之流體;出流段流態發展區 190是連通於出流段整流器150和出流口 130之間’其可緩衝流入和 流出振動腔室110之流體。進流段流態發展區180與出流段流態發展 區190,經研究後發現,其可降低工作流體流入進流口 120或者流出 出流口 130之流阻,也就是由於進流口 120與出流口 130的低流阻, 因此工作流體可以很容易的流入進流口 120,也可以很容易的排出出 流口 130,故可有效地增加從振動腔室110輸送到出流口 130的流體 的流量,從而提升微繁浦100的整體輸送流量。 進流段流態發展區18〇與出流段流態發展區190還可以抑制振動 腔室之流體回流(back flow)現象,防止回流流至進流口 120或者出流口 130 ’且進流段流態發展區180與出流段流態發展區190 ’其分別又連 接進流段整流器140與出流段整流器150,可提供由振動腔室no擠 壓變形時於進流口 120處所誘發之渦旋充份發展其流態,故還具有流 體緩衝、暫存之功用。 藉由改變進流段流態發展區180與出流段流態發展區19〇在進流 段與出流段串接數量的不同,或者,改變在進流段與出流段上尺寸的 大小,也可造成流阻上的不對稱性而有類似整流器之效果,配合振動 薄膜週期性之運動(排出和吸入模式),微幫浦因而有淨流量的產生。 進流段流態發展區180與出流段流態發展區19〇的幾何尺寸除了 可以提升流體傳輸效能外,亦是影響系統共振頻的主要因素之一,此 可提供設計者直觀的共翻設計參數,且可藉由_接—個到數 個不等之;磁發展區得顺幫浦㈣之各式工作鱗,關應使用者 端不同之需求。 值得注意的是,當致動器17〇往復作動時,經由流場可視化印⑽ )技術可以觀察到’在振動腔室ιι〇之麵入口⑴與 201226309 腔體出口 m處會分別存在有第一流體渦輯ρι與第二流體渦旋對 F2,如第圖所示,當致動器17〇於共振頻下往復作動時,藉由進 流段流態發展區⑽和出流段流態發展區⑽麟計,振動⑽室⑽ 内之流體難㈣和F2㈣制完錢展,讀於進概體交換與 傳送’因而可以大幅提升薄膜式微鶴1()()之流體傳輸效率。 此設計概念與先前技術以壓力差為主要考量因素有著截然不同 之差異’本發明在織腔室11叫提供額外之空間(即職段流態發展 區⑽和出流段流態發展區19〇),作為流場内渴漩對之發展區,當渦 旋在進流段流態發展區180和出流段流態發展區19〇之中完全發展 後,可以使振動腔室110内之流體渦漩對F1和F2加速達到完全發展 之狀態,從而將提升薄膜式微幫浦100之整體傳輸流量(discharge)。 請繼續參閱第1C圖,值得注意的是,在前述實施例中,進流口 之中心線與入口緩衝區之壁面法線之夾角均為0。,但並不僅侷限於 此’只要介於±90。即可;出流口之中心線與出口緩衝區之壁面法線之 炎角均為0° ’但並不僅揭限於此,只要介於土9〇。即可;例如,第】c 圖中,進流口之中心線C3與進流段流態發展區之中心線α之夾角φ 約為45°,而出流口之中心線C4與出流段流態發展區之中心線C2之 夾角Ψ約為45° ;此外,進流段流態發展區與出流段流態發展區之中 心線夾角α並不限定於180°,只要介於±180。即可,第1C圖揭示了夾 角α為45°之情況。 第二實施例 請參閱第2Α圖及第2Β圖,其揭示的薄膜式微型幫浦200主要包 括有振動腔體210、進流口 220、出流口 230、進流段連通器240、出 流段連通器250、振動薄膜260、致動器270、進流段流態發展區280 及出流段流態發展區290。 201226309 進流口 220是連接於進流段流態發展區内,其用以銜接外部 輸送管路,以垂直或水平的方絲人流體;出加⑽是連接於出流 段流態發福290内’其用靖接外部輸送管路,可以垂直或水平的 方式導出流體。 如第2B _示’振動_ 是設置於振動腔體細之上。致動 器27〇是連接於振動薄膜,其用於振動_ 進行往復振動; 致動器270較佳地可以是堡電元件、電磁驅動元件、熱驅動元件、氣 動薄膜元件、機械振動元件或熱氣驅動元件。舉例來說,當致動器27〇 為壓電元件時,藉域電元件之往復侧,即可麟振麟膜產 生往復擴張贿壓之變形,進而達成纖_ 產錄復振動之效 果。 如刖所述,當致動器270驅使振動薄臈260進行往復振動時,振 動腔體加之内部空間或體積即可產生往復的增大與縮小。更詳細的 說,虽振動薄膜260向上運動(吸入模式)時,振動腔體21()内之壓力會 低於外界壓力而產生負壓狀態,因而使得流體經由進流口 22〇、入口 渦/旋發展280、出流段流態發展區290和出流口 230被吸入至振動腔 體210内;反之,當振動薄膜26〇向下運動(排出模式)時,振動腔體 210内之壓力會高於外界壓力,因而使得流體經由進流口 22〇、進流段 流態發展區280、出流段流態發展區290和出流口 230流出振動腔體 210。當致動器270往復作動時,進流段流態發展區280内之流體渦漩 對F2’將流體導入振動腔體21〇,而振動腔體21〇内之流體渦旋對F1, 則將由進流段流態發展區所流入之流體導引至出流段流態發展區 290 ’最後出流段流態發展區29〇内之流體渦漩對F3,將流體導引至出 流口 230 ;藉由進流段流態發展區28〇和出流段流態發展區29〇的幾 何大小的不對稱之設計,可達到一類似整流器之效果而有淨流量產 -11 - 201226309 生。 進流段連通器240是用來連接於振動腔體210與進流段流態發展 區280,其用以匯整並傳輸於進流段流態發展區280及振動腔體210 間往復來回流動之流體;出流段連通器250是用來連接於振動腔體21〇 與出流段流態發展區290 ’其用以匯整並傳輸於振動腔體21〇及出流 段流態發展區290間往復來回流動之流體。 進流段連通器24〇與出流段連通器250,亦可如第一實施例所揭 露,較佳地為整流器,以對工作流體提供方向性流阻,用以加強該薄 膜式微幫浦之流體指向性,更進一步地提升該薄膜式微幫浦之運作效 鲁 能。 廣義來說,進流段連通器24〇和出流段連通器25〇可以以不具流 體導引性(flowdirecting)之流道存在,舉例來說,一截面積固定之直線 机道’如第2A圖所示。而此連通器亦可採用整流器之設計,經由改 隻其幾何形狀設計,而使得流阻具有方向性,可進一步提升薄膜式微 幫浦之運作效能。更具體而s,進流段連通器可設計為一從進流 段流態發展區28〇往振動腔體逐漸擴大之形狀,而出流段連通器 亦可採用-從振動腔體21M主出口緩_ 29〇逐漸擴大之形狀。# 田振動;|膜26〇向上運動(吸入模式)時,對於流體經由進流段連通器 相較於經由出流段連通n 25〇至振動腔體洲之流動而言,其流 阻較小’反之,當振動薄膜26〇向下運動(排出模式)時,對於流體由 振動腔體210經由出流段連通器25〇才目較於經由進流段整流器之 流,而言’其流阻較小,因而使流體的指向性獲得提升,可加強薄膜 式微幫4 之運作效能。本實關之進流段連勒及出流段連通器 :可以採用特斯拉閥或其他任何可達成流阻具有差異性之結構及處 理(如表面親疏水處理)。 12- 201226309 進流段流態發展區280是連接於進流段連通器240與振動腔體21〇 之間’其可緩衝流入和流出振動腔體210之流體;出流段流態發展區 290是連接於出流段連通器250與振動腔體210之間其可緩衝流入和 流出振動腔體2!0之流體。在第二實施例之中,進流段流態發展區28〇 與出流段流態發展區290兩者具有不同的大小,但在第一實施例之 中’進流段流態發展區180與出流段流態發展區19〇兩者是具有相同 的大小。 第三實施例 請參閱第3A圖及第兕圖,其揭示的薄膜式微幫浦3〇〇主要包括 有振動腔體310、進流口 320、出流口 330、第一進流段連通器M〇a、 第二進流段連通器340b、第一出流段連通器350a、第二出流段連通器 350b、第二出流段連通器35〇c、振動薄膜36〇、致動器wo、進流段流 態發展區380、第一出流段流態發展區39〇a及第二出流段流態發展區 390b。 進流口 320是連接於與第一進流段整流器34〇a,其用以銜接外部 輸送管路,以垂直或水平的方式導入流體;出流口 33〇是連接於與第 二出流段連通器350c,其用以銜接外部輸送管路,以垂直或水平的方 式導出流體。 如第邛圖所示,振動薄膜360是設置於振動腔體31〇之上。致動 器37〇是連接於振動薄膜360,其用於振動薄膜36〇進行往復振動, 致動器370較佳地可以是壓電元件、電磁驅動元件、熱驅動元件、氣 動薄膜元件、機械振動元件或熱氣驅動元件。舉例來說,當致動器37〇 為壓電7G件時,藉由壓電元件之往復伸縮,即可使得振動_36〇產 生往復擴張與擠壓之變形’進而達成振動薄膜36〇產生往復振動之效 果。 a -13- 201226309 如前所述,當致動器370驅使振動薄膜360進行往復振動時,振 動腔體310之内部空間或體積即可產生往復的增大與縮小。更詳細的 說’當振動4膜360向上運動(吸入模式)時,振動腔體⑽内之壓力會 低於外界壓力而產生負壓狀態,因而使得流體經由進流口 32〇、進流 段流態發展區380、第一出流段流態發展區39〇a、第二出流段流態發 展區390b和出流口 330被吸入至振動腔體31〇内;反之,當振動薄膜 360向下運動(排出模式)時,振動腔體31〇内之壓力會高於外界壓力, 因而使得流體經由進流口 320、進流段流態發展區380、第一出流段流 態發展區390a、第二出流段流態發展區39〇b和出流口 33〇流出振動腔 體310。當致動器370往復作動時,進流段流態發展區38〇内之流體 渦旋對F2”將流體導入振動腔體31〇,振動腔體31〇内之流體渦漩對 F1”順勢將流體導入第一出流段流態發展區390a,第一出流段流態發 展區390a内之流體渦漩對F3”和F4”兩者互相交流,將流體再導入第 二出流段流態發展區390b,第二出口緩衝區390b内之流體渦漩對F5” 將流體導入出流口 330 ;藉由於振動腔體310兩侧設置不同緩衝區數 量(以第3A圖為例,一入口緩衝區38〇和兩出口緩衝區39〇a、390b的 不對稱設計),此幾何結構的不對稱可達到類似整流器之效果而有淨流 量產生,以達成薄膜式微幫浦300之運作功能。 第一進流段連通器340a是連接於進流段流態發展區380與進流口 320之間,其用以匯整並緩衝於進流口 32〇及進流段流態發展區380 間往復來回流動之流體;第二進流段連通器340b是連接於振動腔體 310與入口渦漩區380之間,其用以匯整並緩衝於振動腔體310及進 流段流態發展區380間往復來回流動之流體。 第一出流段連通器350a是連接於振動腔體310與第一出流段流態 發展區380a之間’其用以匯整並緩衝於振動腔體310及第一出流段流 201226309 態發展區380a間往復來回流動之流體;第二出流段連通器35〇b是連 接於第一出流段流態發展區380a與第二出流段流態發展區380b之 間,其用以匯整並緩衝於第一出流段流態發展區3S0a及第二出流段流 態發展區380b間往復來回流動之流體;第三出流段連通器35〇c是連 接於第二出流段流態發展區380b與出流口 330之間,其用以匯整並緩 衝於第二出流段流態發展區380b及出流口 330間往復來回流動之流 體》 廣義來說,進流段連通器340a、340b和出流段連通器35〇a、350b、 350c可以以不具流體導引性(也挪也江由屯)之流道存在,舉例來說,一 截面積固定之直線流道,如第3A圖所示。而此連通器亦可採用整流 器之設計,經由改變其幾何形狀設計,而使得流阻具有方向性,以提 升薄膜式微幫浦之運作效能。更具體而言,在如第3C圖所示之薄膜 式微幫浦300中,第一進流段連通器34〇a具有從進流口 32〇往入口緩 衝區380逐漸擴大之形狀’第二進流段連通器34〇b具有從進流段流態 發展區380往振動腔體31〇逐漸擴大之形狀;而第一出流段連通器35〇& 具有從振動腔體310往第一出流段流態發展區39〇a逐漸擴大之形狀, 第二出流段it通器现具有從第一出流段流態發展區施往第二出 流段流態發展區鳥逐漸敍之職,第三丨流段連聽班具有 從第-出流段流態發展區39%往出流口 33()逐麵大之形狀。當振動 薄膜36〇向上運動(吸入模式)時,對於流體經由第一進流段連通器遍 和第-進献連職34Gb她於經由第—丨流段連顧35Ga、第二 出流4又連通€ 35Gb和帛二丨流段i^通m至振動腔體训之流動 而s ’其"_L阻較小,反之,當振動薄膜36〇向下運動(排出模式)時, 對於流體由振動腔體31〇經由第一出流段連通器施、第二出流段連 通器35〇b彳n流段連通^娜。彳目較於經由第—進流段連通器 -15- 201226309 34〇a和第一進流段連通器34〇b之流動而言,其流阻較小,因而使流 體的指向性獲得提升,可加強薄膜式微幫浦3〇〇之運作效能。本實施 例之進流段連通器及出流段連通器亦可以採用特斯拉閥或其他任何 可達成流阻具有差異性之結構及處理(如表面親疏水處理)。 進流段流態發展區380是連接於第一進流段連通器34〇&和第二進 流段連通器340b之間’其可緩衝流入和流出振動腔體31〇之流體;第 一出流段流態發展區390a是連接於第一出流段連通器35〇&和第二出 流段連通器350b之間,其可緩衝流入和流出振動腔體31〇之流體;第 二出流段流態發展區390b是連接於第二出流段連通器35〇b和第三出 流段連通器350c之間,其可緩衝流入和流出振動腔體31〇之流體。 另外’進流段流態發展區和出流段流態發展區設置數量的不同除 了可以使流道具有流體指向性外,此一設計可得到一較寬廣的流量高 峰效能曲線。多個進流段流態發展區和出流段流態發展區亦可因需求 不同,而有不同之流態發展區幾何形狀設計。 第四實施例 請參閱第4A圖及第狃圖,其揭示的薄膜式微幫浦4〇0主要包括 有第一振動腔體4l〇a、第二振動腔體410b、進流口 42〇、出流口 430、 第一進流段連通器440a、第二進流段連通器440b、第一出流段連通器 450a、第二出流段連通器450b、第三出流段連通器45〇c、第一振動薄 膜460a、第二振動薄膜460b、第一致動器470a、第二致動器470b、 進流段流態發展區480及出流段流態發展區490。 進流口 420是連接於第一進流段連通器440a,其用以銜接外部輸 送管路,以垂直或水平的方式導入流體;出流口 430是連接於第三出 流段連通器450c,其用以銜接外部輸送管路,以垂直或水平的方式導 出流體。 201226309 如第4B圖所示,第一振動薄膜彻a是設置於第一振動腔體㈣ 之上’第二振動薄膜佩是設置於第二振動腔體儀之上第一致 動器佩是連接於第—娜_條,其麟第—躺祕4·進 行往復振動。第二致動器俱是連接於第二振動薄膜樞,其用於 第二振動_娜進行往復振動,第一致動$伽和第二致動器儀 較佳地可以是壓電元件、電磁驅動元件、熱驅動元件、氣動薄膜元件、 機械振動元件或熱氣鶴播;糊綠,當帛―贿和第二 致動器47〇b為-壓電元件時,藉由壓電元件之往復伸縮,即可使得第 -振動薄膜條和第二振動細佩產生往缝張與纏之變形, 進而達成第一振動薄膜460a和第二振動薄膜46〇b產生往復振動之效 果。而因應使用端不同之需求’可調變兩致動器(第一致動器儀和 第二致動器470b)回往復振動之相位差來改變傳輸效率。 亦可因需求不同而使用多個致動器(兩個以上的致動器),藉由控 制各致動器的作動時序,亦可達一流體傳輸目的,此即為世人所熟稔 之螺動式微幫浦的作動原理’而進流段流態發舰和出流段流態發展 區之概念亦可用於此類微幫浦,作為提升微幫浦效能方法之一,並非 僅僅侷限於無閥式微幫浦上而已。 如前述,當第一致動器470a和第二致動器470b分別驅使第一振 動薄膜460a和第二振動薄膜460b進行往復振動時,第一振動腔體41〇a 和第二振動腔體41〇b之内部空間或體積即可產生往復的變大與縮 小。更详細的說,若第一致動器47〇a和第二致動器47〇b兩者為同相 振動,當第一振動薄膜460a和第二振動薄膜46〇b向上運動(吸入模式) 時,第一振動腔體4l〇a和第二振動腔體4l〇b内之壓力會低於外界壓 力而產生負壓狀態,因而使得流體經由進流口 42〇、進流段流態發展 區480、出流段流態發展區490和出流口 430被吸入至第一振動腔體 -17- 201226309 410a和第二振動腔體奶此内;反之,當第一振動薄膜恥〜和第二振 動薄膜460b向下運動(排出模式)時,第一振動腔體41〇a和第二振動腔 體410b内之壓力會高於外界壓力,因而使得流體經由進流口 42〇、進 流段流態發展區480、第一出流段流態發展區49〇a和出流口 43〇流出 第一振動腔體410a和第二振動腔體奶此。當第一振動腔體41〇a和第 二振動腔體410b往復作動時,進流段流態發展區48〇内之流體渦旋對 將流體導入第一振動腔體4l〇a,第一振動腔體410a内之流體渦漩對則 接著將流體導入第二振動腔體41〇b,第二振動腔體410b内之流體渦 漩對兩者互相作用’將流體再導入出渦旋發展區490,出流段流態發 展區490内之流體渦漩對將流體導入出流口 43〇 ;藉由進流段流態發 展區480、出流段流態發展區490的不對稱設計,可使其具有流體指 向性而有淨流量產生’以達成薄膜式微幫浦400之運作功能。 第一進流段連通器440a是連接於進流段流態發展區480與進流口 420之間,其用以匯整並緩衝於進流口 42〇及進流段流態發展區48〇 間往復來回流動之流體;第二進流段連通器44〇b是連接於振動腔體 410與進流段流態發展區480之間,其用以匯整並緩衝於第一振動腔 體410a及入口緩衝區480間往復來回流動之流體。 第一出流段連通器450a是連接於第一振動腔體410a與第二振動 腔體410b之間,其用以匯整並緩衝於第一振動腔體4〗〇a及第二振動 腔體410b間往復來回流動之流體;第二出流段連通器450b是連接於 第二振動腔體410b與出流段流態發展區480之間,其用以匯整並緩衝 於第二振動腔體410b及出流段流態發展區480間往復來回流動之流 體;第三出流段連通器450c是連接於出流段流態發屐區480與出流口 430之間,其用以匯整並緩衝於出流段流態發展區480及出流口 430 間往復來回流動之流體。 201226309 廣義來說’進流段連通器440a、440b和出流段連通器45〇a、Μ% 45〇c可以不具流體導引性(fl〇wdirectin幻之流道形式存在,舉例來說, 一截面積固定之直線流道’如第4A圖所示。而此連通器亦可採用整 流器之設計,經由改變其幾何形狀設計,而使得流阻具有方向性以 提升薄膜式微幫浦之運作效m具體而言,第—進流段連通器*他 具有從進流口 420往進流段流態發展區48〇逐漸擴大之形狀,第二進 流段連通器440b具有從進流段流態發展區48〇往第一振動腔體41以 逐漸擴大之形狀;而第一出流段連通器450a具有從第一振動腔體41以 往第二振動腔體4l〇b逐漸擴大之形狀,第二出流段連通器45此具有 從第二振動腔體41〇b往出流段流態發展區49〇逐漸擴大之形狀,第三 出流段連通器450c具有從出流段流態發展區49〇往出流口 43〇逐漸擴 大之形狀。舉例來說,t第-振動薄膜條和第二振動薄膜概向 上運動(吸入模式)時,對於流體經由第一進流段連通器44〇&和第二進 流段連通器440b相較於經由第一出流段連通器45〇a、第二出流段連 通器450b和第二出流段連通器450c至第一振動腔體4施和第二振動 腔體410b之流動而言,其流阻較小;反之,冑第一振動薄膜條和 第二振動薄膜460b向下運動(排出模式)時,對於流體由第一振動腔體 410a和第二振動腔體410b經由第一出流段連通器45%、第二出流段 連通器450b和第三出流段連通器450c相較於經由第一進流段連通器 440a和第一進流段連通器440b之流動而言,其流阻較小,因而使流 體的指向性獲得提升,可加強薄膜式聽浦·之運作效能。本實施 例之進流段連通器及出流段連通器亦可以採用特斯拉閥或其他任何 可達成流阻具有差異性之結構及處理(如表面親疏水處理)。 進流段流態發展區480是連接於第一進流段連通器私以和第二進 流段連通器樓之間,其可緩衝流人和流出第—振動腔體她及第 201226309 二振動腔體410b之流體;出流段流態發展區49〇是連接於第二出流段 連通器450b和第三出流段連通器450c,其可緩衝流入和流出第一振 動腔體410a及第二振動腔體41〇b之流體。 此外’進流段流態發展區、出流段流態發展區及振動腔體可採用 不同的配置方式以因應使用端各種不同工作曲線需求之應用。舉例來 說,進流段流態發展區480或出流段流態發展區490之任一者或兩者 可置放於兩振動體之間,如第4C圖、第4D圖所示。 更具體而言’以第4C圖為例,由進流口 420至出流口 430,其配 置方式依序為進流段流態發展區480連接於第一進流段連通器440a和 第二進流段連通器44〇b之間;第一振動腔體41〇a連接於第二進流段 連通器440b和第一出流段整流器450a之間;而出口緩衝區490則連 接於第一出流段連通器450a和第二出流段連通器45〇b之間;最後, 第二振動腔體41 Ob則連接於第二出流段連通器45〇b和第三出流段連 通器450c之間。 第五實施例 請參閱第5A圖及第5B圖,其揭示的薄膜式微幫浦5〇〇主要包括 有振動腔體510、第一進流口 520a、第二進流口 520b、出流口 530、 第一進流段連通器540a、第二進流段連通器54〇b、第三進流段連通器 540c、第四進流段連通器540d、第一出流段連通器550a、第二出流段 連通器550b、振動薄膜560、第一進流段流態發展區58〇a、第二進流 段流態發展區580b及出流段流態發展區590。 第一進流口 52〇a是連接於第一進流段連通器540a,其用以銜接外 部輸送管路’以垂直或水平的方式導入流體;第二進流口 520b是連接 於第三進流段連通器540c,其用以銜接外部輸送管路,以垂直或水平 的方式導入流體;出流口 530是連接於第二出流段連通器55〇b,其用 201226309 以銜接外職送管路,以《或斜財式導出流體。 致動器57〇是連接於振動薄膜,其用於振動薄膜⑽進行往 復振動,致動器別較佳地可以是壓電元件、電磁驅動元件、熱驅動 兀件、氣動_元件、機械振動元件或減軸元件。舉例來說當 致動器57〇為麈電元件時,藉由壓電元件之往復伸縮,即可使得振動 薄膜560產生往復擴張與擠壓之變形,進而達成振動_ 產生往 復振動之效果。 如别所述,當致動器570驅使振動薄臈56〇進行往復運動時,振 動腔體510之内部空間或體積即可產生往復的增大與縮小。更詳細的 說’當振動薄膜56〇向上運動(吸入模式)時,振動腔體⑽内之壓力會 低於外界壓力而產生負壓狀態,因而使得兩流體分別經由第一進流口 520a、第二進流口 520b、第一進流段流態發展區58以和第二進流段流 態發展區580b、出流段流態發展區590和出流口 53〇被吸入至振動腔 體510内;反之,當振動薄膜56〇向下運動(排出模式)時,振動腔體 510内之壓力會高於外界壓力,因而使得流體經由第一進流口 52〇a、 第二進流口 52〇b、第一進流段流態發展區58〇a、第二進流口 52〇b、出 流段流態發展區590和出流口 530流出振動腔體510。當振動腔體51〇 往復作動時’第一進流段流態發展區580a内之流體渦旋對和第二進流 段流態發展區580b内之流體渦旋對將流體導入振動腔體51〇,振動腔 體510内之流體渦漩對將流體導向出流口 530 ;藉由第一進流段流態 發展區580a和第二進流段流態發展區580b的幾何形狀與大小的不對 稱設計’可使得兩進流口至振動腔體之流道上有不同之流阻大小,因 而使得第一進流口 520a和第二進流口 520b可以導入不等比例之兩種 流體,達到特定比例之流體混合作用;同時,也因為入口、出口渦璇 發展的幾何不對稱性,亦使流道設計具有流體指向性而有淨流量往出 -21 - 201226309 流口 53〇流動,以達成薄膜式微幫浦500之運作功能。 第一進流段連通器540a是連接於第一進流段流態發展區58〇a與 第一進流口 52〇a之間,其用以匯整並緩衝於第一進流口 52〇a及第一 進流段流態發展區580a間往復來回流動之流體;第二進流段連通器 540b是連接於振動腔體510與第一進流段流態發展區58〇a間往復來回 流動之流體;第三進流段連通器540c是連接於第二進流段流態發展區 58〇b與第一進流口 52〇b之間,其用以匯整並緩衝於第二進流口 52〇c 及第二進流段流態發展區580b間往復來回流動之流體;第四進流段連 通器540d是連接於振動腔體510與第二進流段流態發展區58〇b之 · 間,其用以匯整並緩衝於振動腔體510及第二進流段流態發展區58〇b 間往復來回流動之流體。 第一出流段連通器550a是連接於振動腔體51〇與出流段流態發展 區590之間,其用以匯整並緩衝於振動腔體51〇及出流段流態發展區 590間往復來回流動之流體;第二出流段連通器55〇b是連接於出流段 流態發展區’與出流口 53〇之間,其用以匯整並緩衝於出流段流態 發展區590及出流口 530間往復來回流動之流體。 廣義來說’進流段連通器54〇a、M〇b、54〇c、M〇d和出流段連通 籲 器55〇a、550b可以以不具流體導引性(fl〇wdirecting)之流道形式存在, 舉例來說,一截面積固定之直線流道,如第5A圖所示。而此連通器 亦可制m之設計,經纽變錢何形狀設計,峨得流阻具有 方向性’以提升薄膜式微幫浦之運作效能。更具體而言,第一進流段 連通器540a具有從第一進流口 52〇a往第一進流段流態發展區58加逐 漸擴大之形狀’第二進流段連通器5她具有從第一進流段流態發展區 5S〇a往振動腔體510逐漸擴大之形狀,第三進流段連通器74〇c具有從 第-進流口 52〇b往第二進流段流態發展區遞逐漸擴大之形狀,第 -22- 201226309 四進流段連通器540d具有從第二進流段流態發展區580b往振動腔體 510逐漸擴大之形狀;而第一出流段連通器550a具有從振動腔體51〇 往出流段流態發展區590出流口 530逐漸擴大之形狀,第二出流段連 通器550b具有從出流段流態發展區590往出流口 53〇逐漸擴大之形 狀。 舉例來說’當振動薄膜560和向上運動(吸入模式)時,對於流體 經由第一進流段連通器54〇a、第二進流段連通器540b、第三進流段連 通器540c、第四進流段連通器54〇d相較於經由第一出流段連通器 55〇a、第二出流段連通器55〇b至振動腔體51〇之流動而言,其流阻較 小;反之,當振動薄膜500向下運動(排出模式)時,對於流體由振動 腔體510經由第一出流段連通器55〇a、第二出流段連通器55此相較於 經由第一進流段連通器54〇a、第二進流段連通器Mob、第三進流段連 通器540c、第四進流段連通器54〇d之流動而言,其流阻較小,因而 使流體的指向性獲得提升,可加強薄膜式微幫浦5⑻之運作效能。本 實知例之H段H ^及&流段整流II亦可以採用特斯拉閥或其他 任何可軸颇具有差紐之結構及處理(如表面親疏水處理)。 第-進流段流態發展區58〇a是連接於第一進流段連通器5他和 第二進流段連通n遍之間,其可緩衝流入和流出振動腔體51〇之流 體;第二進流段流態發展區寫是連接於第三進流段連通器慨和 第四進流段連通器54〇d之間,其可緩衝流入和流出振動腔體51〇之流 體。 請繼續參閱第5C ,亦可採用多個進流段流態發展區及多個出 流段渦璇發舰Μ存在,並以進流段流態發舰和城段流態發展 區的設置數量不同或入、出口渦旋發展的幾何形狀不同,除了可以提 升溥膜式微幫浦500之運作效能外,更可達到流體混合和分配等一連 -23- 201226309 串的操控動作。具體來說,如第5C圖,第一進流段流態發展區580a 之中心線C6與振動腔體入口侧之中心線CIO之夾角βΐ約為45。,第 二進流段流態發展區580b之中心線C7與振動腔體入口側之中心線 C10之夾角β2約為45。;而出流段流態發展區之中心線C8和C9與振 動腔體出口側之中心線C11之夾角γΐ和γ2約為45。。其_,第一進流 段流態發展區580a和第二進流段流態發展區580b用於同時引入兩流 體進入振動腔體510,用以增加進入振動腔體510之流量及進行流體 混合之功用。出流段流態發展區用於引導流體由振動腔體510往第一 出流口 530a、第二出流口 530b流出,除了提昇流體傳輸效能外,亦 具有流體分配之功用。 第六實施例 請參閱第6圖,其揭示的薄膜式微幫浦600主要包括有振動腔體 610、進流口 620、出流口 630、進流段連通器640、出流段連通器650、 振動薄膜(設於振動腔體之上,未示於圖中)、進流段流態發展區680、 出流段流態發展區690、兩個第一導流部613、兩個第二導流部614、 進流導流部6幻、第一出流導流部691及兩第二出流導流部692,其中 第一導流部613係對稱於腔體入口 611,並且係位於腔體入口 611附 近,用以減少流體往進流口流動;第二導流部614係對稱於腔體出口 612,並且係為振動腔體側壁之一部份,增加流體往出流口流動,,用 以提供朝向出流口方向一正向流體淨流量;進流導流部681是用來導 引由進流口流往振動腔體610之設計,第一出流導流部691是導引流 體從振動腔體610流至出流口 630,第二出流導流部692則是用來減 少流體往回流至振動腔體610。 進流口 620是連接於進流段流態發展區680内’其用以銜接外部 輸送管路,以垂直或水平的方式導入流體;出流口 630是連接於出流 201226309 段流態發展區690内,其用以銜接外部輸送管路,以垂直或水平的方 式導出流體。 如前所述,當致動器(設於振動薄膜之上,未示於圖中)驅使振動 薄膜進行往復振動時,振動腔體610之内部空間或體積即可產生往復 的增大與縮小。更詳細的說,當振動薄膜向上運動(吸入模式)時,振 動腔體610内之壓力會低於外界壓力而產生負壓狀態,因而使得流體 經由進流口 620、入口渦漩發展680、出流段流態發展區<390和出流口 630被吸入至振動腔體610内;反之,當振動薄膜向下運動(排出模式) 時’振動腔體610内之壓力會高於外界壓力,因而使得流體經由進流 口 620、進流段流態發展區680、出流段流態發展區690和出流口 630 流出振動腔體610。當致動器往復作動時,進流段流態發展區680内 之流體渦旋對將流體導入振動腔體610,而振動腔體610内之流體渦 旋對則將由進流段流態發展區所流入之流體導引至出流段流態發展 區690,最後出流段流態發展區690内之流體渦旋對將流體導引至出 流口 630 ;藉由進流段流態發展區680和出流段流態發展區69〇的幾 何大小的不對稱之設計,可達到一類似整流器之效果而有淨流量產 生。 進流段連通器640是用來連接於振動腔體610與進流段流態發展 區680,其用以匯整並傳輸於進流段流態發展區68〇及振動腔體61〇 間往復來回流動之流體;出流段連通器65〇是用來連接於振動腔體61〇 與出流段流態發展區690,其用以匯整並傳輸於振動腔體61〇及出流 段流態發展區690間往復來回流動之流體。 廣義來說,進流段連通器640和出流段連通器650可以以不具流 體導引性(flowdirecting)之流道存在,舉例來說,一截面積固定之直線 流道,如第6圖所示。而此連通器亦可採用整流器之設計,經由改變 -25- 201226309 其幾何形狀設計,而使得流阻具有方向性,可進一步提升薄膜式微幫 浦之運作效能。更具體而言,進流段連通器64〇可設計為一從進流段 机態發展區680往振動腔體610逐漸擴大之形狀,而出流段連通器砧〇 亦可採用一從振動腔體610往出口緩衝區69〇逐漸擴大之形狀。當振 動薄骐向上運動(吸人模式)時’對於流體經由進流段整越_相較 於經由出流段整流器650至振動腔體61〇之流動而言,其流阻較小; 反之,當振動薄膜向下運動(排出模式)時,對於流體由振動腔體61〇 經由出流段連通器650相較於經由進流段連通器64〇之流動而言,其 流阻較小,因而使流體的指向性獲得提升,可加強薄膜式微幫浦600 之運作效能。本實施例之進流段連通器及出流段連通器亦可以採用特 斯拉閥或其條何可達成雜具有差紐之賴及處理(如表面親疏 水處理)。 進流段流態發展區680是連接於進流段整流器64〇與振動腔體61〇 之間,其可緩衝流入和流出振動腔體61〇之流體;出流段流態發展區 690是連接於出流段整流器65〇與振動腔體61〇之間其可緩衝流入和 流出振動腔體610之流體。 此外,進流段流態發展區中心線Cl2與出流段流態發展區之中心 線CI3爽角α並不限定於⑽。,只要介於士⑽。即可,第石圖為夹角^ 為45°之情況。第六實施例的特點在於針對渦漩發展之特性分別在振 動腔體610、進流段流態發展區68〇、出流段流態發展區69〇分別加入 一種以上的導流部,使流場内之渦漩能有更完整之發展,此一概念皆 可應用在前述的第-縣五之實關上,而使微健之顏傳輸效率 獲得更一進一步之提升。 總結言,本發明為機械薄膜式微幫浦振動腔體之創新設計,可以 有效提升微幫浦效率,並增加可傳輸的流體流量,還可廣泛與其他各 -26- 201226309 種薄膜式微㈣作接細深具發展與錢上之潛力。 實施方4 ⑴一種微型幫浦,用以輸送一工作流體,其包括:一振動腔室, 用以容納該工作流體;一進流口與一出流口,其分別與該振動腔室相 連通,供該工作流體經由該進流口流入該振動腔室並經由該出流口流 出该振動腔室;以及一第一流態發展區,其具有一流態發展空間供該 工作流體發展其流態,雜紐室係經由該第—赫發廳與該進流 口或者該出流口相連通。 (2) 如第⑴實施方式所述之微型幫浦,還包括:一第二流態發展 區,其具有一流態發展空間供該工作流體發展其流態,該振動腔室係 經由该第二流態發展區與該進流口或者該出流口相連通。 (3) 如第⑺實施方式所述之微型幫浦,還包括:一振動薄膜,其 设置於該振動腔室之上;一致動器,其與該振動薄膜相接觸,係用以 驅動該振動薄膜使其進行往復運動,以驅使該工作流體經由該進流口 流入該振動腔室並經由該出流口流出該振動腔室;以及一第一連通元 件與第一連通元件,該振動腔室經由該第一連通元件以及該第二連 通元件而分別與該第一流態發展區與該第二流態發展區相連通。 (4) 如第(1)實施方式所述之微型幫浦’其中該第一連通元件與該 第二連通元件為一整流器,其可對該工作流體提供一方向性流阻,該 整流器為一喷嘴、一擴散器、一特斯拉閥、一親水表面或者一疏水表 面。 ⑸如第(1)實施方式所述之微型幫浦,其中該進流口和該出流口 係以垂直或水平的方式將工作流體導出。 (6)如第(1)實施方式所述之微型幫浦,其中該致動器為一壓電元 件、一電磁驅動元件、一熱驅動元件、一氣動薄膜元件、一機械振動 -27- 201226309 元件或一熱氣驅動元件。 ⑺如第⑴實施方式所述之微型幫浦,其中該第一流態發展區或 該第二流態發展區中心線與該振動腔室中心線之間的夾角係介於〇° 〜360°之間。 (8) 如第(1)實施方式所述之微型幫浦,其中該進流段整流器中心 線與該第一流態發展區壁面法線之間的夾角係介於0°〜360°之間’該 出流段整流器中心線與該第二流態發展區壁面法線之間的夾角係介 於0°〜360°之間。 (9) 如第⑴實施方式所述之微型幫浦,其中該進流口中心線與該 修 第一流態發展區壁面法線之間的夾角係介於〇。~360°之間,該出流口 中心線與該第二流態發展區壁面法線之間的夾角係介於〇。〜36〇。之 間’進流口之中心線與第一或第二流態發展區中心線之間的夾角係介 於0°〜360°之間’出流口之中心線與第一或第二流態發展區中心線之 間的夾角係介於0°〜360°之間。 (10) —種微幫滤,用以輸送一流體,其包括:一進口與一出口; 一流態發展區,其具有一流動發展空間供該流體發展其流態;以及一 振動腔體,其經由該流態發展區與該進口或者該出口相連通並容納且 · 驅動該流體。 本案實為一難得一見,值得珍惜的難得發明,惟以上所述者,僅 為本發明之最佳實關而已,當不能以之限定本發明所實施之範圍。 即大凡依本發明f請專利侧所作之鱗變化與_,賴仍屬於本 發明專利涵蓋之範_ ’謹請責審查委㈣鑑,並祈惠准,是所至 禱0 【圖式簡單說明】 -28- 201226309 f1A、iimic圖係為本發明第—實施例之示意圖; 第2A與2B®係為本發明第二魏例之示意圖; 第3A與3B®係為本㈣第三實補之示意圖,· 第4A、4B、4C與4D圖係為本發明第四實施例之示意圖; 第5A、5B與5C圖係為本發明第五實施例之示意圖;以及 第6圖係為本發明第六實施例之示意圖。201226309 VI. Description of the invention: [Technical field to which the invention pertains] The present invention refers to a kind of non-dispensing micro-push, especially - a thief without a reading micro-[previous technique] Can be divided into two types: face and non-mechanical. The biggest advantage of mechanical micro-help is limited by special red fluid, which depends on the actuator ___ each design; the surface-type gang is based on the nature of its working fluid, such as electrophoresis, electro-osmosis The formula is only _ with a charge or a polar molecule X for the seam, which is low, usually requires a large working voltage. Other micro-pulls such as bubble type, magnetic power type, etc. There are restrictions on its application. In the mechanical micro-pump, the film displacement type (referred to as the thin film type) accounts for the majority of the 'mainstream of the current research. If the literature and patent search for the micro-pull navigation parts and valves, it can be found that "Electric" is the field of production and research in various types of actuators. If the type depends on the type, the piezoelectric micro-pull can be divided into two categories: "existing type" and "no valve type". It can be divided into two types: silk with _ with passive width, _ in the near scale has been riding a man», the light research has been trending towards f°, and the number of patent-free pieces without valve is less than other valves. Type, but because of its simple structure: 'No = parts and no need to consume energy and no, blocking and other issues, has become the mainstream of academic research in recent years' shows that the valveless micro-pull is still in the nascent development period, with high development The space of sex and invention. The valveless pump of the diffuser/nozzle geometry proposed by Stemme et al., US Patent No. US62〇329i, et al. (Tu Zhikai, “New Type No Valve 201226309 Micro-Pulse Development” The Master's thesis of the Institute of Applied Mechanics, National Taiwan University, 2004) also proposes a one-piece valveless micro-pull design. In 2005, Ng et al., Singapore, proposed the use of a wing shape in US Patent No. US691〇869. The airfoil) is used for the design of the pump runner, and in 2006 Izzo et al. (Ivano l2zo, Dino Accoto, Arianna Menciassi, Lothar Schmitt, Paolo Dario, <{Modeling and experimental validation of a piezoelectric micropump with novel no-moving-part valves^, Sensors and Actuators A-Physical, Vol. L33: 128-140, 2007) Changing the geometry of the diffuser/nozzle' allows fluid directivity to be improved. In the same year, Y〇on et al. (jae Sung Yoon, Jong Won Choi, II Hwan Lee, Min Soo Kim, eiA valveless micropump for bidirectional applications", Sensors and Actuators A-Physical, Vol.  135: 833-838, 2〇07) proposes another innovative valveless design and proposes that this pump has dual-direction fluidity. It is clear from the above literature that the study of valveless pumps is currently very popular. Theme of. At present, the valveless micro-pull can be mainly divided into the following four categories: (1) Nozzle/diffuser: the difference between the smaller flow resistance (forward) and the larger flow resistance (reverse) with divergence, The net flow rate, which accounts for about 6〇% of the valveless micro-pull design, is currently the main valveless research theme. (2) Main and side branch runners: This type of design is based on the difference in flow resistance between the main and side branch runners. For example, the ride is carried out by the Wei (4) inspection, and the straight flow path is forward. The flow resistance is small, and the flow channel is added to the entanglement to cause a difference between the forward and reverse, which accounts for about 15% of the valveless micro-pump design, as disclosed in U.S. Patent No. 5,876,187. In addition, in the 6-year γ〇〇η proposed in the straight flow channel plus the side branch channel to connect the vibration cavity to achieve the design of the asymmetric structure; and f try to reverse the series of two micro-pulls The purpose of two-way transport of fluids. 201226309 (3) Block type: Adding people in the straight flow channel (_, wing body), which is the extension deformation design of the nozzle/diffusion it, which accounts for 5% of the valveless micro-pull design. (4) vascular flow: in the mammal _ fetal _, has not yet developed, the blood in the vascular towel is also a flawless concept, that is, at the asymmetry point of the flow channel structure Point shouting volume production such as ___, accounting for about 15% of the valveless micro-pull design. % The above-mentioned various types of valveless micro-pull research focuses on the design and optimization of rectifiers (4) and (4), while the shadows of other parts are rarely added and discussed. The reason is that there is no thief. Gu is the pressure of the rectifier for one week (four) compared with the «money to the money ^ net ^, and the purpose of fluid transmission; so in the past no-valve micro-pull research, all from the pressure point of view of other departments The function of the component, such as the vibration, is only considered to provide the rectifier-pressure source, and the fluid and the outlet are only considered as interfaces to communicate with the outside world. In the following year, Higashi et al. proposed a new valveless drive concept in the US patent. The rectifier is designed to be connected to the short-long asymmetric flow path on both sides of the vibrating cavity. Then use a pressure change source with an asymmetric duty cycle (ie, a _ not equal to 5 〇 /.) to achieve flow, and a buffer is proposed in the New Zealand patent (pressure absorption _ design concept can improve the scale of fluid transmission, However, its starting point is still in line with the past (four) general force scale squad, _, did not really consider the impact of changes in the flow field of other components other than the rectifier. 2 〇〇 9 years by Wang et al (Xie Mingzhe, "no valve Research on the Design and Actuation Mechanism of Micro-Pulse Cavity", Master's thesis of Taiwan University's Institute of Fine Mechanics 2_) proposed a new type of micro-pull cavity design, which found that there is a nucleus flow field. However, the development of the engraving flow field and the performance of the micro-pump have significant and highly relevant characteristics. According to this-vortex development, the flow guiding element is added in the vibrating cavity, so that the micro (four) efficiency is significantly improved. In view of this, the applicant After careful experimentation and research, and I have never thought of the case, I have finally conceived the case of "Micro-Pu Pu", and overcoming the above shortcomings, the town is a brief description. 'Invention> The present invention is in the fluid inlet (out) Between the mouth and the rectifier, a proper size and number of "fluid development zones" are added. In the flow development zone, the population is difficult/common and the vortex/vortex can be fully developed, and at the same time, the σ and σ can be reduced. Because the cylinder fluid can easily flow into the inlet, it can also be easily discharged from the outlet, which can greatly improve the fluid transmission efficiency of the pump and increase the flow rate of the delivery flow. The step is designed and changed to a variety of different sizes, sizes, hybrids, _ micro pump working curve, so that the hair _ micro pump has more and more applications. Therefore, according to the invention - envisioning a miniature pump for delivering a working fluid comprising: a vibrating chamber for receiving and driving the working fluid; an inlet port and an outlet port, respectively, and the vibrating chamber Connected to each other Flowing into the vibration chamber through the inlet port and flowing out of the vibration chamber through the outlet port; and a first flow development zone having a first-class development space for the working fluid to develop its flow state, the vibration chamber The chamber is in communication with the inflow port or the outflow port via the first fluid state development zone. Therefore, according to the second concept of the present invention, a micro pump is provided for transporting helium fluid, which includes: an inlet and an inlet An outlet; a first-rate development zone having a flow development space for the fluid to develop its fluid state; a vibrating cavity that communicates with the inlet or the outlet via the fluid development zone and houses and drives the fluid. [Embodiment].  This case will be fully understood by the following examples. Making people who are familiar with the art can be based on Yuan Chengzhi. However, the implementation of this case may not be limited to its implementation by the following implementation cases.  First Embodiment Please refer to Figures 1A and 1B. The micro-pull 1 disclosed therein mainly includes a vibration chamber 110, Inlet port 120, Outlet 130, Inlet section rectifier 14〇, Outlet section rectifier 150, Vibration film 160, Actuator 170, The inflow section fluid state development zone 18〇 and the outflow section fluid development zone 190.  The inlet port 120 is connected to the inflow section fluid state development zone 18〇, It is used to engage the external delivery line' to introduce fluid in a vertical or horizontal manner; The outflow port 13〇 is connected to the outflow section fluid state development zone 190, It is used to connect the external conveying pipeline, The fluid can be exported in a vertical or horizontal manner.  As shown in Figure 1B, The vibrating membrane 16 is disposed above the vibrating chamber 11〇; The actuator Π0 is connected to the diaphragm 1 (30, It is used for vibrating film 16 〇 for reciprocating vibration,  The actuator 170 preferably may be a piezoelectric element, Electromagnetic drive components, Thermal drive components, Air moving film element, Mechanical vibration element or hot gas drive element; for example, When the actuator 17 is a piezoelectric element, By reciprocating expansion and contraction of the piezoelectric element, The diaphragm 16 can be deformed by reciprocating expansion and extrusion. Further, the vibrating film 16 is reciprocated (m: Iprocatingmotion), Thereby, the fluid in the vibrating chamber 11 is moved.  As mentioned earlier, When the actuator Π0 drives the diaphragm 16 to reciprocate, The internal space or volume of the vibration chamber 110 can produce a reciprocating increase and decrease. In more detail, When the vibrating membrane 160 moves upward (inhalation mode), The pressure in the vibration chamber 11〇 will be lower than the external pressure to generate a negative pressure state. Thus the fluid is passed through the inlet port 12〇, Inflow 201226309 section of the development zone 180, The outflow section fluid state development zone 19〇 and the outflow port 130 are drawn into the vibration chamber 110; on the contrary, When the vibrating membrane 160 moves downward (discharge mode), The pressure in the vibration chamber 110 will be higher than the external pressure' thus causing fluid to pass through the inlet port 120,  Inflow section fluid state development zone 180, The outflow section fluid state development zone 190 and the outflow port 130 exit the vibration chamber 110.  The inlet section rectifier 140 is connected between the vibration chamber 110 and the inflow section fluid development zone 18〇. The fluid used to collect and buffer the flow back and forth between the inflow section fluid development zone 180 and the vibrating chamber no; The outflow section rectifier 150 is connected between the vibration chamber ι1 〇 and the biL state development zone 190. It is used for collecting and buffering between the vibration chamber 11 〇 and the outflow section fluid development zone 190. Fluid The inlet section rectifier and the outflow section rectifier are designed to change their geometry, And the flow resistance is directional, To enhance the operational efficiency of the thin film micro-pull. The inflow section rectifier M0 and the outflow section rectifier 15 are connected as a connecting element. The inlet port 120 and the outlet port 130 are in communication with the vibration chamber 110 via two communication members, respectively.  More specifically, The inflow section rectifier M0 has a shape that gradually expands from the in-flow state development zone 18 to the vibration chamber 110. The outflow section rectifier 15 has a shape that gradually develops from the vibration chamber 110 in the inflow section. When the vibrating membrane moves upward (inhalation mode), For fluid flow through the inflow section rectifier (10) compared to the flow through the outflow section rectifier 150 to the vibrating chamber g 11〇, Its flow resistance is small; on the contrary, When the vibration film _ moves downward (discharge mode), For fluid flow from the vibrating chamber ιι via the outflow section rectifier 150 compared to the flow through the inflow section rectifier 14 Its flow resistance is small,  Therefore, the operational efficiency of the micro-pull is achieved. In the embodiment of the present invention, the rectifier and the rectifying section of the outlet section can also be used for the nozzle, Royal ^, It is possible to achieve a structure and treatment with different flow resistance (such as surface sulfur hydrophobic treatment).  The inflow section fluid state development zone 180 is connected between the inflow section rectifier U0 and the inlet port 120 201226309, It can buffer fluid flowing into and out of the vibration chamber 110; The outflow section fluid state development zone 190 is in communication with the outlet section rectifier 150 and the outlet port 130 which buffers fluid flowing into and out of the vibrating chamber 110. Inflow section fluid state development zone 180 and outflow section fluid state development zone 190, After research, it was found that It can reduce the flow resistance of the working fluid flowing into the inflow port 120 or out of the outflow port 130, That is, due to the low flow resistance of the inlet port 120 and the outlet port 130,  Therefore, the working fluid can easily flow into the inlet port 120, It is also easy to discharge the outlet 130. Therefore, the flow rate of the fluid delivered from the vibration chamber 110 to the outflow port 130 can be effectively increased. Thereby increasing the overall conveying flow of the micro-powder 100.  The flow regime of the inflow section 18〇 and the outflow section fluid development zone 190 can also suppress the back flow of the vibrating chamber. The return flow is prevented from flowing to the inflow port 120 or the outflow port 130' and the inflow section fluid state development zone 180 and the outflow section fluid state development zone 190' are respectively connected to the inflow section rectifier 140 and the outflow section rectifier 150, It is possible to provide a vortex induced by the vortex at the inlet port 120 when the vibration chamber is squeezed and deformed to develop its flow state. Therefore, it also has a fluid buffer, The function of temporary storage.  By changing the inflow section fluid state development zone 180 and the outflow section fluid state development zone 19〇 in the inflow segment and the outflow segment in series, the number of connections is different, or, Change the size of the inflow and outflow segments, It can also cause asymmetry in the flow resistance and has a similar rectifier effect. Cooperate with the periodic movement of the diaphragm (discharge and suction mode), The micro-pull thus has a net flow.  In addition to improving the fluid transmission efficiency, the geometry of the inflow section fluid state development zone 180 and the outflow section fluid state development zone It is also one of the main factors affecting the resonant frequency of the system. This provides the designer with an intuitive set of design parameters. And can be connected by _ to several; The magnetic development zone has a variety of working scales from Shun Pump (4). Respond to the different needs of the user.  It is worth noting that When the actuator 17 is reciprocating, According to the flow field visual printing (10) technique, it can be observed that there is a first fluid vortex and a second fluid vortex pair F2 respectively at the surface entrance (1) of the vibration chamber and the outlet outlet m of the 201226309. As shown in the figure, When the actuator 17 reciprocates at a resonance frequency, With the inflow section fluid state development zone (10) and the outflow section fluid state development zone (10), The fluid in the vibration (10) room (10) is difficult (4) and F2 (4) to complete the money exhibition. Reading in the general body exchange and transmission 'thus can greatly improve the fluid transmission efficiency of the film type micro crane 1 () ().  This design concept is quite different from the prior art in that the pressure difference is the main consideration factor. The present invention provides additional space in the weaving chamber 11 (ie, the stage flow development zone (10) and the outflow section fluid state development zone. ), As a development zone in the flow field, When the vortex is fully developed in the inflow section fluid state development zone 180 and the outflow section fluid state development zone 19〇, The fluid vortex in the vibration chamber 110 can accelerate the F1 and F2 to a fully developed state. Thereby, the overall transmission capacity of the thin film micro pump 100 will be increased.  Please continue to refer to Figure 1C. It is worth noting that In the foregoing embodiment, The angle between the center line of the inlet and the wall normal of the inlet buffer is zero. , But it is not limited to this as long as it is between ±90. Yes; The angle between the center line of the outflow port and the wall normal of the exit buffer is 0°', but it is not limited to this. As long as it is between 9 土. Yes; E.g, In the figure c, The angle φ between the center line C3 of the inlet port and the center line α of the flow development zone of the inflow section is about 45°. The angle Ψ between the center line C4 of the outflow port and the center line C2 of the outflow section fluid development zone is about 45°; In addition, The angle α between the flow development zone of the inflow section and the fluid development zone of the outflow section is not limited to 180°. As long as it is between ±180. Yes, Fig. 1C shows the case where the angle α is 45°.  Second Embodiment Please refer to Figure 2 and Figure 2, The thin film micro-pump 200 disclosed therein mainly includes a vibration cavity 210, Inlet 220, Outlet 230, Inflow section connector 240, Outlet section connector 250, Vibration film 260, Actuator 270, The inflow section fluid state development zone 280 and the outflow section fluid state development zone 290.  201226309 Inlet port 220 is connected to the inflow section fluid development zone. It is used to connect the external conveying line, a vertical or horizontal square wire human fluid; The addition (10) is connected to the outflow section of the flow state of the welfare 290. The fluid can be exported vertically or horizontally.  For example, the 2B_showing 'vibration _ is set on the fine portion of the vibrating cavity. The actuator 27 is connected to the diaphragm, It is used for vibration _ to perform reciprocating vibration;  The actuator 270 can preferably be a fort electrical component, Electromagnetic drive components, Thermal drive components, Air moving film element, Mechanical vibration element or hot gas drive element. for example, When the actuator 27 is a piezoelectric element, By the reciprocating side of the domain electrical component, The Lin Zhenlin film can produce the deformation of the reciprocating expansion bribe pressure. In turn, the effect of recording the vibration of the fiber is achieved.  As stated, When the actuator 270 drives the vibrating diaphragm 260 to reciprocate, The vibration chamber plus the internal space or volume can produce a reciprocating increase and decrease. In more detail, Although the vibrating film 260 moves upward (inhalation mode), The pressure in the vibrating cavity 21 () will be lower than the external pressure to generate a negative pressure state. Thus the fluid is caused to flow through the inlet 22 Entrance vortex/spin development 280, The outflow section fluid state development zone 290 and the outflow port 230 are drawn into the vibration chamber 210; on the contrary, When the vibrating membrane 26 is moved downward (discharge mode), The pressure in the vibrating cavity 210 will be higher than the external pressure. Thus the fluid is caused to flow through the inlet 22 Inflow section, fluid development zone 280, The outflow section fluid state development zone 290 and the outflow port 230 exit the vibrating cavity 210. When the actuator 270 is reciprocating, The fluid vortex in the inflow section fluid development zone 280 introduces fluid into the vibrating cavity 21〇 to F2', And the fluid vortex in the vibration chamber 21 is vortexed to F1,  The fluid flowing in from the inflow section fluid development zone is directed to the fluid vortex pair F3 in the outflow section fluid development zone 290 'the last outflow section fluid development zone 29 〇, Directing fluid to the outflow port 230; By the asymmetric design of the geometry of the inflow section, the development zone 28〇 and the outflow section fluid development zone, A similar rectifier effect can be achieved with a net flow rate of -11 - 201226309.  The inflow section communicater 240 is for connecting to the vibrating cavity 210 and the inflow section fluid state development zone 280. The fluid used to be collected and transported back and forth between the inflow section fluid state development zone 280 and the vibrating cavity 210; The outflow section connector 250 is connected to the vibrating chamber 21〇 and the outflow section fluid state development zone 290' for rectifying and transporting between the vibrating cavity 21〇 and the outflow section fluid state development zone 290 Fluid flowing back and forth.  Inflow section connector 24〇 and outflow section connector 250, It can also be as disclosed in the first embodiment. Preferably a rectifier, To provide directional flow resistance to the working fluid, To enhance the fluid directivity of the thin film micro-pump, Further improve the operational efficiency of the thin film micro-pull.  Broadly speaking, The inflow section communicater 24〇 and the outflow section linker 25〇 may exist in a flow path that does not have fluid directing. for example, A straight line with a fixed area is shown in Figure 2A. The connector can also be designed with a rectifier. By changing its geometry design, And the flow resistance is directional, It can further enhance the operational efficiency of the thin film micro-pull. More specific and s, The inlet section communicater can be designed to have a shape that gradually expands from the inflow section fluid state development zone 28 to the vibration chamber. The outflow section connector can also adopt a shape that gradually expands from the main outlet of the vibration chamber 21M. #田振动; | When the membrane 26〇 moves upward (inhalation mode), For the flow of fluid through the inflow section communicater compared to the flow through the outflow section n 25〇 to the vibrating cavity body, Its flow resistance is small', conversely, When the vibrating membrane 26 is moved downward (discharge mode), For the flow of fluid from the vibrating cavity 210 via the outflow section communicater 25, it is compared to the flow through the inflow section rectifier, In terms of 'the flow resistance is small, Thereby improving the directivity of the fluid, It can enhance the operation efficiency of the thin film micro-help 4. The inlet section of the actual section and the outlet section of the outlet section: It is possible to use a Tesla valve or any other structure and treatment that can achieve flow resistance differences (such as surface hydrophobic treatment).  12-201226309 The inflow section fluid state development zone 280 is connected between the inflow section interconnector 240 and the vibrating cavity 21'' to buffer the fluid flowing into and out of the vibrating cavity 210; The outflow section fluid state development zone 290 is connected between the outflow section communicater 250 and the vibrating cavity 210 to buffer the inflow and outflow of the vibrating cavity 2! 0 fluid. In the second embodiment, The inflow section fluid state development zone 28〇 and the outflow section fluid state development zone 290 have different sizes, However, in the first embodiment, both the inflow section fluid state development zone 180 and the outflow section fluid state development zone 19〇 have the same size.  Third Embodiment Please refer to Figure 3A and Figure ,, The thin film micro-push 3〇〇 disclosed therein mainly includes a vibration cavity 310, Inlet 32, Outlet 330, First inflow section connector M〇a,  a second inflow section connector 340b, First outflow section connector 350a, Second outflow section connector 350b, Second outflow section connector 35〇c, Vibration film 36〇, Actuator wo, Inflow section fluid development zone 380, The first outflow section fluid state development zone 39〇a and the second outflow section fluid state development zone 390b.  The inlet port 320 is connected to the first inflow section rectifier 34A, It is used to connect the external conveying line, Introducing fluid in a vertical or horizontal manner; The outflow port 33〇 is connected to the second outflow section communicater 350c, It is used to connect the external conveying pipeline, The fluid is exported in a vertical or horizontal manner.  As shown in the figure, The vibrating membrane 360 is disposed above the vibrating cavity 31〇. The actuator 37 is connected to the vibration film 360, It is used for vibrating film 36〇 for reciprocating vibration,  Actuator 370 can preferably be a piezoelectric element, Electromagnetic drive components, Thermal drive components, Air moving film element, Mechanical vibration element or hot gas drive element. for example, When the actuator 37 is a piezoelectric 7G piece, By reciprocating expansion and contraction of the piezoelectric element, This allows the vibration _36 〇 to produce a reciprocating expansion and deformation of the extrusion ‘and thus achieves the effect of the reciprocating vibration of the vibrating membrane 36 。.  a -13- 201226309 As mentioned earlier, When the actuator 370 drives the vibrating membrane 360 to reciprocate, The internal space or volume of the vibrating cavity 310 can produce a reciprocating increase and decrease. In more detail, when the vibration 4 film 360 moves upward (inhalation mode), The pressure in the vibration chamber (10) will be lower than the external pressure to generate a negative pressure state. Thus the fluid is caused to flow through the inlet 32 Inflow section fluid state development zone 380, The first outflow section fluid state development zone 39〇a, The second outflow section fluid state development zone 390b and the outflow port 330 are drawn into the vibration chamber 31〇; on the contrary, When the vibrating membrane 360 moves downward (discharge mode), The pressure inside the vibrating cavity 31 is higher than the external pressure.  Thus, the fluid is caused to flow through the inlet port 320, Inflow section fluid state development zone 380, The first outflow section fluid development zone 390a, The second outflow section fluid state development zone 39〇b and the outflow port 33〇 exit the vibrating cavity 310. When the actuator 370 is reciprocating, The fluid in the flow regime of the inflow section 38〇 is vortexed to the F2" to introduce the fluid into the vibrating cavity 31〇, The fluid vortex in the vibration chamber 31〇 introduces the fluid into the first outflow section fluid development zone 390a. The fluid vortex in the first outflow section fluid state development zone 390a communicates with each other, F3" and F4", Re-introducing the fluid into the second outflow section fluid development zone 390b, The fluid vortex in the second outlet buffer 390b is directed to F5" to introduce fluid into the outflow port 330; By setting different buffer numbers on both sides of the vibrating cavity 310 (take the 3A picture as an example, An entry buffer 38〇 and two exit buffers 39〇a, 390b asymmetric design), The asymmetry of this geometry can achieve a rectifier-like effect with a net flow. In order to achieve the operational function of the thin film micro-pump 300.  The first inflow section interconnector 340a is connected between the inflow section fluid state development zone 380 and the inflow port 320. It is used to collect and buffer the fluid flowing back and forth between the inflow port 32〇 and the inflow section fluid development zone 380; The second inflow section communicater 340b is connected between the vibrating cavity 310 and the inlet vortex zone 380. It is used to collect and buffer the fluid flowing back and forth between the vibrating cavity 310 and the inflow section fluid development zone 380.  The first outflow section interconnector 350a is connected between the vibrating cavity 310 and the first outflow section fluid state development zone 380a. 'It is used for collecting and buffering in the vibrating cavity 310 and the first outflow section flow 201226309 state a fluid that flows back and forth between development zones 380a; The second outflow section communicater 35〇b is connected between the first outflow section fluid state development zone 380a and the second outflow section fluid state development zone 380b. The fluid used for reciprocating back and forth between the first outflow section fluid state development zone 3S0a and the second outflow section fluid development zone 380b; The third outflow section communicater 35〇c is connected between the second outflow section fluid state development zone 380b and the outflow port 330. It is used to collect and buffer the fluid flowing back and forth between the second outflow section fluid development zone 380b and the outflow port 330. Broadly speaking, Inflow section connector 340a, 340b and the outflow section linker 35〇a, 350b,  The 350c can exist in a flow path that is not fluid-guided (also moved from the river). for example, a straight flow path with a fixed cross-sectional area, As shown in Figure 3A. The connector can also be designed with a rectifier. By changing the geometry of the design, And the flow resistance is directional, In order to improve the operational efficiency of the thin film micro-pull. More specifically, In the thin film micro pump 300 as shown in Fig. 3C, The first inflow section communicater 34A has a shape that gradually expands from the inlet 32 to the inlet buffer 380. The second inflow section 34b has a flow development zone 380 from the inflow section to the vibrating chamber. The shape of the body 31 is gradually enlarged; And the first outflow section connector 35〇&  Having a shape that gradually expands from the vibrating cavity 310 to the first outflow section fluid state development zone 39〇a,  The second outflow section of the iterative device now has a function from the first outflow section fluid state development zone to the second outflow section fluid state development zone. The third turbulent section has a shape from the 39% to the outflow port 33 () of the first-outflow section. When the vibrating membrane 36 is moved upward (inhalation mode), For the fluid through the first inflow section of the communicator and the third-job-job 34Gb, she is connected to the 35Ga via the first turbulent section. The second outflow 4 is in turn connected to the flow of the €35Gb and the second turbulent section i^通m to the vibration chamber body training and s 'the" _L resistance is small, on the contrary, When the vibrating membrane 36 is moved downward (discharge mode),  For the fluid to be applied by the vibrating cavity 31〇 via the first outflow section connector, The second outflow section connector 35〇b彳n is connected to the channel. Compared with the flow through the first-inflow section interconnector -15-201226309 34〇a and the first inflow section interconnector 34〇b, Its flow resistance is small, Therefore, the directivity of the fluid is improved, It can enhance the operation efficiency of the thin film micro-pull. The inlet section and the outlet section of the embodiment may also employ a Tesla valve or any other structure and treatment that can achieve flow resistance (e.g., surface hydrophobic treatment).  The inflow section fluid state development zone 380 is connected to the first inflow section interconnector 34〇& And between the second inflow section communicater 340b' which buffers the fluid flowing into and out of the vibrating cavity 31; The first outflow section fluid state development zone 390a is connected to the first outflow section porter 35〇& Between the second outflow segment connector 350b, It can buffer the fluid flowing into and out of the vibrating cavity 31; The second outflow section fluid state development zone 390b is connected between the second outflow section communicater 35〇b and the third outflow section interconnector 350c. It buffers the fluid flowing into and out of the vibrating cavity 31.  In addition, the difference in the number of flow development zones in the inflow section and the flow development zone in the outflow section can make the flow channel have fluid directivity. This design provides a broad flow peak performance curve. The flow development zone and the outflow section flow development zone of multiple inflow sections may also be different due to different needs. There are different geometry development zones.  Fourth Embodiment Please refer to Figure 4A and Figure ,, The thin film micro pump 4〇0 disclosed therein mainly includes a first vibration cavity 4l〇a, The second vibrating cavity 410b, Inlet 42〇, Outlet 430,  First inflow section connector 440a, a second inflow section connector 440b, First outflow section connector 450a, a second outflow section connector 450b, Third outflow section connector 45〇c, The first vibration film 460a, Second vibrating film 460b, First actuator 470a, Second actuator 470b,  The inflow section fluid state development zone 480 and the outflow section fluid state development zone 490.  The intake port 420 is connected to the first inflow section communicater 440a. It is used to connect the external delivery line, Introducing fluid in a vertical or horizontal manner; The outflow port 430 is connected to the third outflow segment connector 450c. It is used to connect the external conveying pipeline, The fluid is directed in a vertical or horizontal manner.  201226309 As shown in Figure 4B, The first vibrating film is disposed on the first vibrating cavity (4). The second vibrating film is disposed on the second vibrating cavity. The first actuator is connected to the first-strip. It has a reciprocating vibration. The second actuator is connected to the second diaphragm, It is used for the second vibration _ Na to reciprocate vibration, The first aligning gamma and the second actuator are preferably piezoelectric elements, Electromagnetic drive components, Thermal drive components, Pneumatic membrane components,  Mechanical vibration components or hot air cranes; Green, When the bribe and the second actuator 47〇b are - piezoelectric elements, By reciprocating expansion and contraction of the piezoelectric element, The deformation of the first vibrating film strip and the second vibrating fine film to the seam and the wrap is caused.  Further, the effect of the reciprocating vibration of the first vibrating film 460a and the second vibrating film 46b is achieved. The transmission efficiency is changed by the phase difference of the reciprocating vibrations of the two actuators (the first actuator and the second actuator 470b) in response to the different needs of the end.  Multiple actuators (more than two actuators) can also be used depending on the requirements. By controlling the timing of actuation of each actuator, Can also achieve a fluid transmission purpose, This is the operating principle of the screw-type micro-pumps that the world is familiar with. The concept of the flow-state launching and outflow section flow development zones of the inflow section can also be used for such micro-pulls. As one of the ways to improve the efficiency of the micro pump, It's not just limited to the valveless micro-pump.  As mentioned above, When the first actuator 470a and the second actuator 470b respectively drive the first vibration film 460a and the second vibration film 460b to reciprocate, The internal space or volume of the first vibrating cavity 41〇a and the second vibrating cavity 41〇b can be reciprocally enlarged and reduced. In more detail, If both the first actuator 47〇a and the second actuator 47〇b are in-phase vibration, When the first vibrating film 460a and the second vibrating film 46〇b move upward (inhalation mode), The pressure in the first vibrating chamber body 410a and the second vibrating chamber body 410b is lower than the external pressure to generate a negative pressure state. Thus, the fluid is caused to flow through the inlet port 42, Inflow section fluid state development zone 480, The outflow section fluid state development zone 490 and the outflow port 430 are drawn into the first vibrating cavity -17-201226309 410a and the second vibrating cavity body; on the contrary, When the first vibrating film is shame~ and the second vibrating film 460b is moved downward (discharge mode), The pressure in the first vibrating cavity 41a and the second vibrating cavity 410b is higher than the external pressure. Thus, the fluid is caused to flow through the inlet port 42, Inflow section fluid state development zone 480, The first outflow section fluid state development zone 49〇a and the outflow port 43〇 flow out of the first vibrating cavity 410a and the second vibrating cavity body. When the first vibrating cavity 41a and the second vibrating cavity 410b reciprocate, a fluid vortex pair in the flow regime of the inflow section 48〇 introduces the fluid into the first vibrating cavity 4l〇a, The fluid vortex pair in the first vibrating cavity 410a then introduces the fluid into the second vibrating cavity 41〇b, The fluid vortex in the second vibrating cavity 410b interacts with the two to re-introducing the fluid out of the vortex development zone 490, The fluid vortex in the outflow section fluid state development zone 490 introduces fluid into the outflow port 43〇; With the inflow section fluid state development area 480, Asymmetric design of the outflow section fluid state development zone 490, It can be made to have fluid orientation and a net flow rate is generated to achieve the operational function of the thin film micro-pump 400.  The first inflow section communicater 440a is connected between the inflow section fluid state development zone 480 and the inflow port 420. It is used to collect and buffer the fluid flowing back and forth between the inflow port 42〇 and the inflow section fluid development zone 48〇; The second inflow section communicater 44〇b is connected between the vibrating cavity 410 and the inflow section fluid development zone 480. It is used to collect and buffer the fluid flowing back and forth between the first vibrating cavity 410a and the inlet buffer 480.  The first outflow section connector 450a is connected between the first vibrating cavity 410a and the second vibrating cavity 410b. The fluid for collecting and buffering between the first vibrating cavity 4 and the second vibrating cavity 410b to reciprocate back and forth; The second outflow section communicater 450b is connected between the second vibrating chamber body 410b and the outflow section fluid state development zone 480. The fluid is used for collecting and buffering between the second vibrating cavity 410b and the outflow section fluid development zone 480 to reciprocate back and forth; The third outflow section connector 450c is connected between the outflow section fluid state hairpin area 480 and the outflow port 430. It is used to collect and buffer the fluid flowing back and forth between the outflow section fluid state development zone 480 and the outflow port 430.  201226309 Broadly speaking, the inflow segment connector 440a, 440b and outflow section connector 45〇a, Μ% 45〇c can be fluid-free (fl〇wdirectin illusion flow form exists, for example,  A straight flow path having a fixed cross-sectional area is shown in Fig. 4A. This connector can also be designed with a rectifier. By changing the geometry of the design, The flow resistance is directional to enhance the operational efficiency of the thin film micro-pump. Specifically, The first-inflow section interconnector* has a shape that gradually expands from the inflow port 420 to the inflow section fluid development zone. The second inflow section communicater 440b has a shape that gradually expands from the inflow section fluid state development zone 48 to the first vibrating cavity 41; The first outflow section communicater 450a has a shape that gradually expands from the first vibrating cavity 41 to the second vibrating cavity 41bb. The second outflow section communicating member 45 has a shape which gradually expands from the second vibrating cavity body 41b to the outflow section fluid state development zone 49〇. The third outflow section communicater 450c has a shape that gradually expands from the outflow section fluid state development zone 49 to the outflow port 43. for example, When the t-vibrating film strip and the second vibrating film are moved upward (inhalation mode), For fluid passing through the first inflow section communicater 44〇& Compared with the second inflow section communicater 440b, via the first outflow section communicater 45a, For the flow of the second outflow section connector 450b and the second outflow section connector 450c to the first vibrating cavity 4 and the second vibrating cavity 410b, Its flow resistance is small; on the contrary, When the first vibrating film strip and the second vibrating film 460b move downward (discharge mode), For the fluid from the first vibrating cavity 410a and the second vibrating cavity 410b via the first outflow segment connector 45%, The second outflow section communicater 450b and the third outflow section communicater 450c are compared to the flow through the first inflow section interconnector 440a and the first inflow section interconnector 440b, Its flow resistance is small, Therefore, the directivity of the fluid is improved, It can enhance the operational performance of the thin film type. The inlet section and the outlet section of the embodiment may also employ a Tesla valve or any other structure and treatment that can achieve flow resistance (e.g., surface hydrophobic treatment).  The inflow section fluid state development zone 480 is connected between the first inflow section communicater and the second inflow section of the interconnector. It can buffer the flow of the person and the fluid flowing out of the first vibration chamber and the vibration chamber 410b of the 201226309; The outflow section fluid state development zone 49 is connected to the second outflow section communicater 450b and the third outflow section interconnector 450c, It can buffer the fluid flowing into and out of the first vibration chamber 410a and the second vibration chamber 41〇b.  In addition, the inflow section fluid development zone, The flow development zone and the vibration chamber of the outflow section can be configured in different ways to meet the needs of various working curves of the end. for example, Either or both of the inflow section fluid state development zone 480 or the outflow section fluid state development zone 490 may be placed between the two vibrating bodies. As shown in Figure 4C, Figure 4D shows.  More specifically, taking the 4C figure as an example, From the inlet 420 to the outlet 430, The configuration manner is that the inflow section fluid state development area 480 is connected between the first inflow section interconnector 440a and the second inflow section interconnector 44〇b; The first vibrating cavity 41〇a is connected between the second inflow section communicater 440b and the first outflow section rectifier 450a; The exit buffer 490 is connected between the first outflow section interconnector 450a and the second outflow section interconnector 45〇b; At last,  The second vibrating chamber 41 Ob is coupled between the second outflow section communicater 45b and the third outflow section coupler 450c.  Fifth Embodiment Please refer to Figures 5A and 5B. The thin film micro-pull 5 disclosed therein mainly includes a vibration cavity 510, First inlet 520a, Second inlet 520b, Outlet 530,  First inflow section connector 540a, Second inflow section connector 54〇b, Third inflow section connector 540c, a fourth inflow section connector 540d, First outflow section connector 550a, Second outflow section connector 550b, Vibration film 560, The first inflow section fluid state development area 58〇a, The second inflow section fluid state development zone 580b and the outflow section fluid state development zone 590.  The first inflow port 52〇a is connected to the first inflow segment connector 540a, It is used to connect the external delivery line 'to introduce fluid in a vertical or horizontal manner; The second inflow port 520b is connected to the third inflow segment connector 540c, It is used to connect the external conveying pipeline, Introducing fluid in a vertical or horizontal manner; The outflow port 530 is connected to the second outflow section communicater 55〇b, It uses 201226309 to connect the external service pipeline. Export fluids in either "or".  The actuator 57 is connected to the diaphragm, It is used for vibrating film (10) for repetitive vibration, The actuator may preferably be a piezoelectric element, Electromagnetic drive components, Heat-driven components, Pneumatic Components, Mechanical vibration element or shaft reduction element. For example, when the actuator 57 is a neon element, By reciprocating expansion and contraction of the piezoelectric element, The vibration film 560 can be deformed by reciprocating expansion and extrusion. In turn, the vibration _ is achieved.  As stated, When the actuator 570 drives the vibrating diaphragm 56 to reciprocate, The internal space or volume of the vibrating cavity 510 can produce a reciprocating increase and decrease. In more detail, when the vibrating membrane 56〇 moves upward (inhalation mode), The pressure in the vibration chamber (10) will be lower than the external pressure to generate a negative pressure state. Thus, the two fluids are respectively passed through the first inlet port 520a, Second inlet 520b, The first inflow section fluid state development zone 58 and the second inflow section fluid state development zone 580b, The outflow section fluid state development zone 590 and the outflow port 53〇 are drawn into the vibration cavity 510; on the contrary, When the vibrating membrane 56 is moved downward (discharge mode), The pressure in the vibrating cavity 510 is higher than the external pressure. Thus, the fluid is caused to pass through the first inlet port 52〇a,  Second inlet port 52〇b, The first inflow section fluid state development area 58〇a, Second inlet port 52〇b, The outflow section fluid state development zone 590 and the outflow port 530 exit the vibrating cavity 510. When the vibrating cavity 51 is reciprocating, the fluid vortex pair in the first inflow section fluid state development zone 580a and the fluid vortex pair in the second inflow section fluid state development zone 580b introduce fluid into the vibrating cavity 51. Oh, The fluid vortex in the vibrating cavity 510 directs the fluid to the outflow port 530; The asymmetric design of the geometry and size of the first inflow section fluid state development zone 580a and the second inflow section fluid state development zone 580b can cause different flows in the flow path from the two inlet ports to the vibrating cavity. Resistance size, Therefore, the first inlet port 520a and the second inlet port 520b can be introduced into two fluids of unequal proportions. Achieve a certain proportion of fluid mixing; Simultaneously, Also because of the entrance, The geometric asymmetry of the development of the export vortex, It also makes the flow channel design have fluid directivity and net flow to and from -21 - 201226309 In order to achieve the operational function of the thin film micro pump 500.  The first inflow section interconnector 540a is connected between the first inflow section fluid state development zone 58〇a and the first inflow port 52〇a. The fluid used for reciprocating back and forth between the first inlet port 52〇a and the first inlet section fluid development zone 580a; The second inflow section communicater 540b is a fluid that is connected to the vibrating cavity 510 and flows back and forth between the first inflow section fluid state development zone 58A; The third inflow section interconnector 540c is connected between the second inflow section fluid state development zone 58〇b and the first inflow port 52〇b. The fluid used to flow back and forth between the second inlet port 52〇c and the second inlet section fluid state development zone 580b; The fourth inflow section coupler 540d is connected between the vibrating cavity 510 and the second inflow section fluid state development zone 58〇b. It is used to collect and buffer the fluid flowing back and forth between the vibrating cavity 510 and the second inflow section fluid development zone 58〇b.  The first outflow section communicater 550a is connected between the vibration chamber body 51 and the outflow section fluid state development zone 590. It is used to collect and buffer the fluid flowing back and forth between the vibrating cavity 51〇 and the outflow section fluid development zone 590; The second outflow section communicater 55〇b is connected between the outflow section fluid state development zone ’ and the outflow port 53〇. It is used to collect and buffer the fluid flowing back and forth between the outflow section fluid state development zone 590 and the outflow port 530.  Broadly speaking, the inflow segment connector 54〇a, M〇b, 54〇c, M〇d and the outflow section are connected to the device 55〇a, 550b can exist in the form of a flow channel without fluid guiding (fl〇wdirecting).  for example, a straight flow path with a fixed area As shown in Figure 5A. And this connector can also be designed in m. Through the new currency, the shape design, Chad flow resistance has directionality to enhance the operational efficiency of the thin film micro-pull. More specifically, The first inflow section communicater 540a has a shape that gradually enlarges from the first inflow port 52A to the first inflow section fluid state development zone 58. The second inflow section linker 5 has the first inflow. The shape of the segmental flow development zone 5S〇a gradually expands toward the vibration cavity 510, The third inflow section communicater 74〇c has a shape that gradually expands from the first inflow port 52〇b to the second inflow section fluid state development zone, -22-201226309 The four-inlet section interconnector 540d has a shape that gradually expands from the second inflow section fluid state development zone 580b to the vibrating cavity 510; The first outflow section communicater 550a has a shape that gradually expands from the vibrating cavity 51 to the outflow section fluid development zone 590. The second outflow section coupler 550b has a shape that gradually expands from the outflow section fluid state development zone 590 to the outflow port 53〇.  For example, when the diaphragm 560 and the upward movement (inhalation mode), For the fluid via the first inflow section communicater 54a, a second inflow section connector 540b, The third inflow section connector 540c, The fourth inflow section communicater 54〇d is compared to the first outflow section communicator 55〇a, In terms of the flow of the second outflow section communicating member 55〇b to the vibrating cavity 51〇, Its flow resistance is relatively small; on the contrary, When the vibration film 500 moves downward (discharge mode), For the fluid to pass from the vibrating cavity 510 via the first outflow segment connector 55〇a, The second outflow section communicater 55 is compared to the first inflow section communicater 54A, Second inflow section connector Mob, The third inflow section connector 540c, In terms of the flow of the fourth inflow section connector 54〇d, Its flow resistance is small, Thus increasing the directivity of the fluid, It can enhance the operating efficiency of the thin film micro-pump 5 (8). H segment H ^ and & The flow section rectification II can also be applied to a Tesla valve or any other structure and treatment that can be made with a differential shaft (such as surface hydrophobic treatment).  The first inflow section fluid state development zone 58〇a is connected between the first inflow section interconnector 5 and the second inflow section connected n times. It can buffer the fluid flowing into and out of the vibrating cavity 51; The second inflow section fluid state development zone is written between the third inflow section connector and the fourth inflow section interconnector 54〇d. It buffers the fluid flowing into and out of the vibrating cavity 51.  Please continue to refer to section 5C. It is also possible to use a plurality of inflow section flow development zones and a plurality of outflow sections to have a vortex ship. And the number of ships in the inflow section and the flow development zone of the city segment are different or entered. The geometry of the exit vortex develops differently, In addition to improving the operational performance of the diaphragm-type micro pump 500, It can also achieve a series of control actions such as fluid mixing and distribution. Specifically, As shown in Figure 5C, The angle β ΐ between the center line C6 of the first inflow section fluid state development zone 580a and the center line CIO of the vibration chamber inlet side is about 45. , The angle β2 between the center line C7 of the second inflow section fluid state development zone 580b and the center line C10 of the entrance side of the vibrating cavity is about 45. ; The angles γ ΐ and γ2 between the center lines C8 and C9 of the outflow section fluid development zone and the center line C11 of the exit side of the vibration chamber are about 45. . its_, The first inflow section fluid state development zone 580a and the second inflow section fluid state development zone 580b are used to simultaneously introduce the two fluid bodies into the vibration cavity 510, It is used to increase the flow into the vibration chamber 510 and to perform fluid mixing. The outflow section fluid development zone is for guiding fluid from the vibrating cavity 510 to the first outflow port 530a, The second outflow port 530b flows out, In addition to improving fluid transfer performance, It also has the function of fluid distribution.  Sixth Embodiment Please refer to Figure 6, The thin film micro-pump 600 disclosed therein mainly includes a vibration cavity 610, Inlet 620, Outlet 630, Inflow section connector 640, Outflow section connector 650,  a vibrating membrane (located on the vibrating cavity, Not shown in the figure), Inflow section fluid state development zone 680,  Outflow section fluid development zone 690, Two first flow guiding portions 613, Two second flow guiding portions 614,  Inflow guide 6 a first outflow diversion portion 691 and two second outflow diversion portions 692, The first flow guiding portion 613 is symmetric with the cavity inlet 611. And it is located near the entrance 611 of the cavity. Used to reduce the flow of fluid to the inlet; The second flow guiding portion 614 is symmetrical to the cavity outlet 612, And is part of the side wall of the vibrating cavity, Increase fluid flow to the outflow, , Used to provide a positive fluid flow toward the outlet; The inflow deflecting portion 681 is for guiding the design of the inflow port to the vibrating cavity 610. The first outflow diversion portion 691 is a guide fluid flowing from the vibration chamber 610 to the outflow port 630. The second outflow diversion portion 692 is for reducing the flow of fluid back to the vibrating cavity 610.  The inlet 620 is connected to the inflow section fluid development zone 680, which is used to connect the external delivery line. Introducing fluid in a vertical or horizontal manner; The outflow port 630 is connected to the outflow 201226309 section of the fluid development zone 690. It is used to connect the external conveying pipeline, The fluid is exported in a vertical or horizontal manner.  As mentioned earlier, When the actuator is placed on the vibrating membrane, Not shown in the figure) When the diaphragm is driven to reciprocate, The internal space or volume of the vibrating cavity 610 can produce a reciprocating increase and decrease. In more detail, When the vibrating membrane moves upward (inhalation mode), The pressure in the vibration chamber 610 is lower than the external pressure to generate a negative pressure state. Thus, the fluid is caused to flow through the inlet 620, Entrance vortex development 680, Outflow section fluid development zone <390 and the outflow port 630 are drawn into the vibrating cavity 610; conversely, when the vibrating membrane moves downward (discharge mode), the pressure in the vibrating cavity 610 is higher than the external pressure, thereby causing the fluid to flow through the inflow The port 620, the inflow section fluid state development zone 680, the outflow section fluid state development zone 690, and the outflow port 630 exit the vibrating cavity 610. When the actuator reciprocates, the fluid vortex in the inflow section fluid development zone 680 directs the fluid into the vibrating cavity 610, and the fluid vortex pair in the vibrating cavity 610 will be from the inflow section fluid state development zone. The inflowing fluid is directed to the outflow section fluid state development zone 690, and the fluid vortex in the last outflow section fluid state development zone 690 directs the fluid to the outflow port 630; The geometrical asymmetry of the 680 and the outflow section fluid state development zone can achieve a similar rectifier effect and a net flow generation. The inflow section interconnector 640 is configured to be coupled to the vibrating cavity 610 and the inflow section fluid state development zone 680 for being integrated and transported between the inflow section fluid state development zone 68 and the vibrating cavity 61. The fluid flowing back and forth; the outflow section communicater 65 is connected to the vibrating cavity 61〇 and the outflow section fluid state development zone 690 for collecting and transporting to the vibrating cavity 61〇 and the outflow section flow The development zone 690 reciprocates back and forth fluid flow. Broadly speaking, the inflow section interconnector 640 and the outflow section interconnector 650 may be present in a flow path that is not fluid directing, for example, a straight flow path having a fixed cross-sectional area, as shown in FIG. Show. The connector can also be designed with a rectifier. By changing the geometry of the -25-201226309, the flow resistance is directional, which further enhances the operation efficiency of the thin film micro-pull. More specifically, the inflow section connector 64 can be designed to gradually expand from the inflow section development region 680 to the vibrating cavity 610, and the outflow section connector anvil can also adopt a slave vibrating chamber. The body 610 is gradually enlarged in the exit buffer zone 69. When the vibrating diaphragm moves upward (inhalation mode), the flow resistance is smaller for the fluid to flow through the inflow section than the flow via the outflow section rectifier 650 to the vibrating cavity 61〇; When the vibrating membrane moves downward (discharge mode), the flow resistance of the fluid from the vibrating chamber 61 via the outflow section communicater 650 is smaller than that of the flow via the inflow section interconnector 64, thus Enhancing the directivity of the fluid enhances the operational performance of the thin film micro-pump 600. The inflow section communicater and the outflow section communicater of this embodiment can also adopt a Tesla valve or a method thereof to achieve the difference and treatment (such as surface dehydration treatment). The inflow section fluid state development zone 680 is connected between the inflow section rectifier 64〇 and the vibrating cavity 61〇, which can buffer the fluid flowing into and out of the vibrating cavity 61〇; the outflow section fluid state development zone 690 is connected Between the outflow section rectifier 65A and the vibrating cavity 61〇, it can buffer the fluid flowing into and out of the vibrating cavity 610. In addition, the center line CI2 of the inflow section fluid development zone and the centerline CI3 refresh angle α of the outflow section fluid development zone are not limited to (10). As long as it is between (10). That is, the stone diagram is the case where the angle ^ is 45°. The sixth embodiment is characterized in that, for the characteristics of the vortex development, one or more flow guiding portions are respectively added to the vibrating cavity 610, the inflow section fluid state development zone 68〇, and the outflow section fluid state development zone 69〇, respectively. The vortex in the field can be more complete development, and this concept can be applied to the above-mentioned first-county five real-time, and the transmission efficiency of the micro-beauty is further improved. In summary, the invention is an innovative design of a mechanical thin film micro-piston vibrating cavity, which can effectively improve the efficiency of the micro-pump and increase the flow rate of the fluid that can be transported, and can also be widely connected with other -26-201226309 kinds of thin film micro (four) The depth of development and the potential of money. Embodiment 4 (1) A micro pump for conveying a working fluid, comprising: a vibrating chamber for accommodating the working fluid; an inflow port and an outflow port respectively communicating with the vibrating chamber Providing the working fluid flowing into the vibration chamber through the inlet port and flowing out of the vibration chamber through the outlet port; and a first fluid development zone having a first-class development space for the working fluid to develop its flow state, The hybrid chamber is connected to the inlet or the outlet via the first-in-a-hair room. (2) The micro pump according to the embodiment (1), further comprising: a second fluid development zone having a first-class development space for the working fluid to develop its fluid state, the vibration chamber being via the second The fluid development zone is in communication with the inlet or the outlet. (3) The micro pump according to the embodiment (7), further comprising: a vibrating film disposed on the vibrating chamber; and an actuator that is in contact with the vibrating film to drive the vibrating The film reciprocates to drive the working fluid to flow into the vibration chamber through the inlet port and out of the vibration chamber through the outlet port; and a first communication element and the first communication element, the vibration The chamber is in communication with the first fluid state development zone and the second fluid state development zone via the first communication element and the second communication element, respectively. (4) The micro-pump of the embodiment (1) wherein the first communication element and the second communication element are a rectifier, which can provide a directional flow resistance to the working fluid, the rectifier being a nozzle, a diffuser, a Tesla valve, a hydrophilic surface or a hydrophobic surface. (5) The micro pump according to the embodiment (1), wherein the inlet port and the outlet port guide the working fluid in a vertical or horizontal manner. (6) The micro pump according to the embodiment (1), wherein the actuator is a piezoelectric element, an electromagnetic driving element, a heat driving element, a pneumatic film element, and a mechanical vibration -27-201226309 Element or a hot gas drive element. (7) The micro pump according to the embodiment (1), wherein an angle between a center line of the first fluid development zone or the second fluidity development zone and a center line of the vibration chamber is between 〇° and 360° between. (8) The micro pump according to the embodiment (1), wherein an angle between the center line of the inlet section rectifier and the wall normal of the first fluid development zone is between 0° and 360° The angle between the center line of the rectifier section rectifier and the wall normal of the second fluid state development zone is between 0° and 360°. (9) The micro pump according to the embodiment (1), wherein an angle between the center line of the inlet and the wall normal of the first fluid development zone is 〇. Between ~360°, the angle between the center line of the outflow port and the wall normal of the second fluid state development zone is between 〇. ~36〇. The angle between the center line of the inlet port and the center line of the first or second fluid state development zone is between 0° and 360°' the center line of the outflow port and the first or second flow state The angle between the centerlines of the development zone is between 0° and 360°. (10) a micro-filter for transporting a fluid, comprising: an inlet and an outlet; a first-stage development zone having a flow development space for the fluid to develop its fluid state; and a vibrating cavity, The fluidic development zone is in communication with the inlet or the outlet and houses and drives the fluid. This case is a rare and rare invention that is worth cherishing, but the above is only the best practice of the present invention, and the scope of the present invention cannot be limited thereto. That is to say, according to the invention, the scale change made by the patent side is _, and Lai still belongs to the scope of the invention patent _ 'Please review the review committee (four), and pray for the right, is the prayer to the zero [simplified description -28- 201226309 f1A, iimic diagram is a schematic diagram of the first embodiment of the invention; 2A and 2B® are schematic diagrams of the second example of the invention; 3A and 3B® are the third (3) third compensation 4A, 4B, 4C, and 4D are schematic views of a fourth embodiment of the present invention; 5A, 5B, and 5C are schematic views of a fifth embodiment of the present invention; and FIG. 6 is a A schematic diagram of a six embodiment.

【主要元件符號說明】 _ :微幫浦 120 =進流口 140 :進流段整流器 160 :振動薄膜 180 =進流段流態發展區 F1 :第一流體渦漩對[Main component symbol description] _ : Micro pump 120 = Inlet 140 : Inlet section rectifier 160 : Vibrating film 180 = Inflow section fluid state development zone F1 : First fluid vortex pair

Cl、C2、¢3、C4 :中心、線 200 : 微型幫浦 220 : 進流口 240 : 進流段連通器 260 : 振動薄膜 280 : 進流段流態發展區 F1,、 F2’、F3’ :流體渦旋對 300 : 微型幫浦 320 =進流口 340a :第一進流段連通器 35〇a :第一出流段連通器 110 :振動腔室 130 :出流口 150 =出流段整流器 170 :致動器 190 :出流段流態發展區 F2 :第二流體渦旋對 Φ、Ψ、α :夾角 210 :振動腔體 230 :出流口 250 :出流段連通器 270 :致動器 290 :出流段流態發展區 310 :振動腔體 330 :出流口 340b :第二進流段連通器 350b :第二出流段連通器 -29- 201226309 350c :第三出流段連通器 370 :致動器 390a :第一出流段流態發展區 36〇 :振動薄膜 380 :進流段流態發展區 390b :第二出流段流態發展區 FI”、F2”、F3”、F4”、F5” :流體渦漩對 4〇〇 :微幫浦 41〇b :第二振動腔體 430 :出流口 44〇b :第二進流段連通器 450b :第二出流段連通器 46〇a :第一振動薄膜 47〇a:第一致動器 480 :進流段流態發展區 5〇〇 :微幫浦 520a :第一進流口 530 =出流口 54〇b :第二進流段連通器 54〇d :第四進流段連通器 550b ··第二出流段連通器 580a:第一進流段流態發展區 590 :出流段流態發展區 C6、C7、C8、C9、CIO、C11 : 6〇〇 :微幫浦 620 :進流口 640 :進流段連通器 680 :進流段流態發展區 4l〇a:第一振動腔體 420 :進流口 44〇a :第一進流段連通器 45〇a :第一出流段連通器 450c :第三出流段連通器 460b :第二振動薄膜 47〇b :第二致動器 490 :出流段流態發展區 510 :振動腔體 520b :第二進流口 540a :第一進流段連通器 540c :第三進流段連通器 550a :第一出流段連通器 560 :振動薄膜 580b :第二進流段流態發展區 βΐ、β2、γΐ、γ2 :夾角 中心線 610 :振動腔體 630 :出流口 650 :出流段連通器 690 :出流段流態發展區Cl, C2, ¢3, C4: Center, line 200: Miniature pump 220: Inlet 240: Inlet section 260: Vibrating membrane 280: Inflow section fluid development zone F1, F2', F3' : Fluid vortex pair 300 : Micro pump 320 = Inlet 340a : First inflow section Communicator 35 〇 a : First outflow section Trunk 110 : Vibrating chamber 130 : Outlet 150 = Outlet Rectifier 170: Actuator 190: Outflow section fluid state development zone F2: Second fluid vortex pair Φ, Ψ, α: Angle 210: Vibrating cavity 230: Outlet 250: Outlet section 270: Actuator 290: outflow section fluid state development zone 310: vibrating cavity 330: outflow port 340b: second inflow section interconnector 350b: second outflow section interconnector -29-201226309 350c: third outflow section Communicator 370: Actuator 390a: first outflow section fluid state development zone 36: vibrating membrane 380: inflow section fluid state development zone 390b: second outflow section fluid state development zone FI", F2", F3 ", F4", F5": fluid vortex pair 4〇〇: micro-pull 41〇b: second vibrating cavity 430: outlet port 44〇b: second inflow section connector 450b: second The flow segment connector 46〇a: the first vibrating membrane 47〇a: the first actuator 480: the inflow section fluid state development zone 5〇〇: the micro pump 520a: the first inflow port 530 = the outflow port 54 〇b: second inflow section communicater 54〇d: fourth inflow section interconnector 550b ··second outflow section interconnector 580a: first inflow section fluid state development zone 590: outflow section flow state development Zone C6, C7, C8, C9, CIO, C11: 6〇〇: Micro pump 620: Inlet 640: Inlet section 680: Inflow section Fluid development zone 4l〇a: First vibrating cavity 420: intake port 44〇a: first inflow section communicater 45〇a: first outflow section communicater 450c: third outflow section interconnector 460b: second vibrating membrane 47〇b: second actuation 490: outflow section fluid state development zone 510: vibrating cavity 520b: second inflow port 540a: first inflow section interconnector 540c: third inflow section interconnector 550a: first outflow section interconnector 560 : vibrating film 580b: second inflow section fluid state development zone βΐ, β2, γΐ, γ2: angled center line 610: vibrating cavity 630: outflow port 650: outflow section connector 690: outflow section flow state development Area

30- 201226309 613 :第一導流部 614 : 681 :進流導流部 691 : 692 :第二出流導流部 611 : 612 :腔體出口 C12 第二導流部 第一出流導流部 腔體入口 C13 :中心線30-201226309 613: first flow guiding portion 614: 681: inflow diversion portion 691: 692: second outflow diversion portion 611: 612: cavity outlet C12 second diversion portion first outflow diversion portion Cavity inlet C13: centerline

Claims (1)

201226309 七、申請專利範圍: 1. 一種微裂幫浦’用以輸送一工作流體’其包括: 一振動腔室,用以容納該工作流體; 一進流口與一出流口,其分別與該振動腔室相連通,供該工作流體經 由該進流口流入該振動腔室並經由該出流口流出該振動腔室;以及 一第一流態發展區,其具有一流態發展空間供該工作流體發展其流 態,該振動腔室係經由該第一流態發展區與該進流口或者該出流口相連 通0 2. 如申請專利範圍第1項所述之微型幫浦,還包括: 一第二流態發展區’其具有一流態發展空間供該工作流體發展其流 態,該振動腔室係經由該第二流態發展區與該進流口或者該出流口相連 通。 3. 如申請專利範圍第2項所述之微型幫浦,還包括: 一振動薄膜’其設置於該振動腔室之上; 一致動器,其與該振動薄膜相接觸,係用以驅動該振動薄膜使其進行 往復運動,以驅使該工作流體經由該進流口流入該振動腔室並經由該出流 口流出該振動腔室;以及 一第一連通元件與一第二連通元件,該振動腔室經由該第一連通元件 以及該第二連通元件而分別與該第一流態發展區與該第二流態發展區相 連通。 4. 如申請專利範圍第!項所述之微型幫浦,其中該第一連通元件與該第 二連通树為-整越,其可觸轉赫提供__方向錢阻,該整 器為—噴嘴、-驗器、—特斯拉閥、—親水表面或者-疏水表面。 5. 如申請專利範圍第t項所述之微型幫浦,其中該進流口和該出流口係 以垂直或水平的方式將工作流體導出。 -32- 201226309 6. 如申凊專利範圍第t項所述之微型幫浦,其中該致動器為一壓電元 件、一電磁驅動元件、一熱驅動元件、一氣動薄膜元件、一機械振動 元件或一熱氣驅動元件。 7. 如申凊專利範圍第i項所述之微型幫浦,其中該第一流態發展區或該 第一流態發展區中心線與該振動腔室中心線之間的夾角係介於〇» 〜360°之間。 8. 如申請專利範圍第!項所述之微型幫浦,其中該進流段整流器中心線 與該第一流態發展區壁面法線之間的夾角係介於〇。〜360。之間,該出 • 流段整流器中心線與該第二流態發展區壁面法線之間的夾角係介於〇 360°之間。 9. 如申請專利範圍第1項所述之微型幫浦,其中該進流口中心線與該第 一流態發展區壁面法線之間的夾角係介於〇。〜360。之間,該出流口中 心線與該第二流態發展區壁面法線之間的夾角係介於〇。〜360。之間, 進流口之中心線與第一或第二流態發展區中心線之間的夾角係介於〇 。〜360°之間’出流口之中心線與第一或第二流態發展區中心線之間的 夾角係介於0°〜360°之間。 φ 10. —種微幫浦,用以輸送一流體,其包括: 一進口與一出口; 一流態發展區,其具有一流動發展空間供該流體發展其流態;以及 一振動腔體,其經由該流態發展區與該進口或者該出口相連通並容納 且驅動該流體。 -33 -201226309 VII. Patent application scope: 1. A micro-cracking pump 'for conveying a working fluid' includes: a vibrating chamber for accommodating the working fluid; an inflow port and an outflow port, respectively The vibration chamber is in communication, the working fluid flows into the vibration chamber through the inlet port and flows out of the vibration chamber through the outlet port; and a first fluid development zone having a first-class development space for the work The fluid develops its fluid state, and the vibrating chamber communicates with the inflow port or the outflow port via the first fluid state development zone. 2. The micro pump as described in claim 1 of the patent scope further includes: A second fluid state development zone has a first-rate development space for the working fluid to develop its fluid state, and the vibration chamber is in communication with the inlet port or the outlet port via the second fluid state development zone. 3. The micro pump of claim 2, further comprising: a vibrating membrane disposed on the vibrating chamber; an actuator that is in contact with the vibrating membrane to drive the The vibrating membrane reciprocates to drive the working fluid to flow into the vibrating chamber through the inlet port and out of the vibrating chamber through the outlet port; and a first connecting member and a second connecting member, The vibration chamber is in communication with the first fluid state development zone and the second fluid state development zone via the first communication element and the second communication element, respectively. 4. If you apply for a patent scope! The micro-pull of the item, wherein the first connecting element and the second connecting tree are -completed, and the tactile hexagram provides a __ direction, and the whole device is a nozzle, a detector, and Tesla valve, - hydrophilic surface or - hydrophobic surface. 5. The micro pump of claim 4, wherein the inlet port and the outlet port direct the working fluid in a vertical or horizontal manner. -32- 201226309 6. The micro pump according to claim t, wherein the actuator is a piezoelectric element, an electromagnetic driving element, a thermal driving element, a pneumatic film element, a mechanical vibration Element or a hot gas drive element. 7. The micro pump of claim i, wherein the angle between the center of the first fluid development zone or the first fluidity development zone and the centerline of the vibration chamber is between 〇» Between 360°. 8. If you apply for a patent scope! The micro pump of the item, wherein an angle between the center line of the inlet section rectifier and the wall normal of the first fluid development zone is between 〇. ~360. The angle between the center line of the flow segment rectifier and the wall normal of the second flow development zone is between 〇360°. 9. The micro pump according to claim 1, wherein the angle between the center line of the inlet and the wall normal of the first-order development zone is 〇. ~360. The angle between the center line of the outlet and the wall normal of the second fluid development zone is between 〇. ~360. The angle between the center line of the inlet and the center line of the first or second fluid development zone is between 〇. The angle between the centerline of the outlet of the ~360° and the centerline of the first or second fluidic development zone is between 0° and 360°. Φ 10. A micro-pump for transporting a fluid comprising: an inlet and an outlet; a first-order development zone having a flow development space for the fluid to develop its fluid state; and a vibrating cavity The fluidic development zone is in communication with the inlet or the outlet and houses and drives the fluid. -33 -
TW099147390A 2010-12-31 2010-12-31 Micro-pump TWI448414B (en)

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Cited By (1)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
TWI565876B (en) * 2015-05-22 2017-01-11 國立臺灣科技大學 Multi-phase drive pump

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SE508435C2 (en) * 1993-02-23 1998-10-05 Erik Stemme Diaphragm pump type pump
US5876187A (en) * 1995-03-09 1999-03-02 University Of Washington Micropumps with fixed valves
US7094040B2 (en) * 2002-03-27 2006-08-22 Minolta Co., Ltd. Fluid transferring system and micropump suitable therefor
SG106067A1 (en) * 2002-03-27 2004-09-30 Inst Of High Performance Compu Valveless micropump

Cited By (1)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
TWI565876B (en) * 2015-05-22 2017-01-11 國立臺灣科技大學 Multi-phase drive pump

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