M306894 八、新型說明： 【新型所屬之技術領域】 係屬ί工程序之液體混合裳4 ’特別是一個應用於廢 水化予處雜序巾德減且無轉之_與污核合裝置。 【先前技術】 化紅料元操倾廢水污染物絲過財，將定量之化 水ΐ並使兩者充分混合，是-個十分常見程序。傳統 ^將ΐ' i分別引人同—槽體中，再利用授摔機械 水k，使兩者均勻混合，此n混合方式，在設 機^槽體以滿足混合反應所需停留時間及需要特定擾拌 t進仃在運轉操作上麵持續耗費電力。為了改善這些 内晨安(GoodMorning)企業，美國Kenics、腦AX、歷& ί H十生產一種名為靜態攪拌管(static Mixer)之混合 器’且普遍應用於化工、醫藥、食品、染料等工業上，此混入裝 置主要應用原理係於管流上游端注人藥臟特 ^ =游^接靜_拌管，减勝管_情接有 &翼’^兩流體沿下射向逐次交叉對分，而達_拌混合效果。 刖述攪拌管内之導翼有許多不同型態，也各自且 L但因f内皆裝有精細、複雜導翼，除製作^本較i外此 用於均勻度較高之流體，若遇有固體或異物流入，極易 U，進岭雜塞’尤其在廢污水處理程柯，更是困難 絲肉’巧’此—㈣之靜_拌管較少被設計於廢污水處理系 ^丨^辰廷有限公⑽發展名為紐混合裝置，般於中民國 寻利么報，公告號第M288200號之新型專利，係於導管内机置兩 Τίί ’流道_有複數相通的通孔及節流片等，使流體能S交互 、過各通孔而產生再混合作用；日本環境科學工業股份有限公司 5 M306894 所發展名為靜止型流體混合裝置，刊登於中民國專利公報，公開 號第00442326號之發明專利，其原理係於圓筒狀殼體内設有多數 之混合小室，並利用錯位配置方式連通各混合小室增加混合效 月b ’以防止流體混合時短路流動所造成的混合不良。前述雖為流 體混合裝置或靜止型流體混合裝置，但其基本原理、應用方式皆 與本裝置明顯然不同。 【新型内容】 鑑於前述問題，本創作僅利用管徑變化造成混合效果，相對 =傳^之攪拌方式可省略桶槽、攪拌機和馬達之設置；相對於其 它靜癌攪拌管而言，則可省略裝置管内導翼，並可減少因異物累 積所造成之阻塞困擾。因此，本創作提供一種低製作成本、低運 ，費用和無阻塞問題之靜態混合裝置概念。特別適合於用水和廢 污水處理工程之化學混凝及酸鹼值調整單元。 x 本，，所提之無阻塞式靜態混合管裝置，是由一個或數個漸 擴與漸縮管串接組合而成。其主要原理係利用流體在通過流管之 =擴時，由於流管斷面加大，造成流體流速降低及流向急速變化， 笞内形成許多不同尺度渦流，使流體產生三維度之混合作用。 — 為了解本創作之功能特性，申請人利用計算流體力學程式進 行電，模擬計算，在相同操作條件下，分析證明本創作的幾種裝 ，所能產生之混合效能，並與未裝置本創作時之直管混合情況進 行比較。模擬結果配合附圖說明如下： 第一圖（a)為未裝置本創作之直管，第一圖（b)、（c)、（d)、 (e)、⑴分別為本創作的五種混合裝置，為了方便模擬比較，本 創作各裝置之水流入口（11)和加藥入口（12)之所有條件均一致。 ，創作裝置之一乃利用一組漸擴漸縮管組合而成，本創作之二則 J將本創作一中之擴縮角度增大而成，裝本創作三為將裝置^創 ^一之擴張後管徑延伸一定長度後再回縮，本創作四為串聯兩組 創作一之擴縮管而成，本創作之五則為串聯兩組本創作三裝置 6 M306894 而成。 算過用:，體⑽進行，模擬計 麻眚於ί取本_五，格賴數為_。。為配人實M306894 VIII. New description: 【New technical field of the invention】 The liquid mixing skirt 4 ′ is a kind of liquid processing program, especially for the application of waste hydration to the sterilized towel. [Prior Art] It is a very common procedure to turn the waste water into the waste of the red material, and to quantify the water and mix the two together. The traditional ^ ΐ i 'i respectively attract the same - the tank body, and then use the mechanical water k to make the two evenly mixed, this n mixing mode The specific disturbances continue to consume electricity during the operation. In order to improve these GoodMorning companies, American Kenics, Brain AX, Calendar & ί H produced a mixer called static mixer (and is commonly used in chemicals, medicine, food, dyes, etc.) Industrially, the main application principle of this mixing device is to inject the medicine at the upstream end of the tube flow. ^^游^接静_mixing tube, win-win tube_情接有&翼'^Two fluids flow down the next direction Divided, and up to _ mix mixed effect. It is stated that there are many different types of guide vanes in the mixing tube, and each of them is also equipped with fine and complex guide vanes. Therefore, in addition to the production of this type, it is used for fluids with higher uniformity. Solid or different flow into, very easy to U, into the Lingchao 'especially in the waste water treatment process Ke, it is more difficult to wire the meat 'Qiao' this - (four) the static _ mixing tube is less designed in the waste water treatment system ^ 丨 ^ Chen Ting Co., Ltd. (10) develops a new name hybrid device, which is similar to the China National Republic of China. It is a new patent for the announcement No. M288200. It is built in the conduit and has two Τίί 'flow channels _ there are complex through holes and sections Flowing the film, etc., so that the fluid can interact with each other and through the through holes to produce a remixing effect; Japan Environmental Science and Industry Co., Ltd. 5 M306894 developed as a static fluid mixing device, published in the Republic of China Patent Gazette, Publication No. 00442326 The invention patent is based on the principle that a plurality of mixing chambers are arranged in the cylindrical casing, and the mixing chambers are connected by a misalignment arrangement to increase the mixing efficiency b' to prevent mixing failure caused by short-circuit flow during fluid mixing. Although the foregoing is a fluid mixing device or a static fluid mixing device, the basic principle and application method are obviously different from the device. [New content] In view of the above problems, the creation only uses the variation of the pipe diameter to cause the mixing effect, and the mixing mode of the relative = transfer can omit the setting of the tank, the mixer and the motor; compared with other static cancer mixing tubes, it can be omitted The inner guide vanes of the device can reduce the blockage caused by the accumulation of foreign matter. Therefore, this creation provides a static mixing device concept with low production cost, low shipping, cost and non-blocking problems. It is especially suitable for chemical coagulation and pH adjustment units for water and wastewater treatment projects. x This, the non-blocking static mixing tube device proposed is a combination of one or several diverging and reducing tubes. The main principle is to use the fluid to expand through the flow tube. Due to the enlarged cross section of the flow tube, the fluid flow velocity is reduced and the flow direction changes rapidly. Many different scale eddy currents are formed in the crucible to make the fluid have a three-dimensional mixing effect. — In order to understand the functional characteristics of this creation, the applicant uses the computational fluid dynamics program to perform electrical and analog calculations. Under the same operating conditions, the analysis proves that several of the creations of the creation can produce mixed effects, and the installation is not installed. The straight tube mixing situation is compared. The simulation results are described below with reference to the following figures: The first figure (a) is a straight tube that is not installed in this creation. The first pictures (b), (c), (d), (e), (1) are the five types of creation. In order to facilitate the simulation comparison, all the conditions of the water inlet (11) and the dosing inlet (12) of each device of the present creation are the same. One of the creation devices is a combination of a set of divergent and divergent tubes. The second part of the creation J is to increase the angle of expansion and expansion of the creation, and the creation of the creation is to create a device. After the expansion, the pipe diameter extends for a certain length and then retracts. This creation is made up of two sets of expansion and contraction tubes. The fifth part of the creation is a series of three sets of 6 M306894. Used to calculate:, body (10), simulation meter paralyzed in ί take this _ five, the number of grid is _. . For the match
5ί=95之污水為5.心配:J ：S ^ L 29 ' 6： s J； 想藥齊^ 整㈣言’加_ G.43%，㈣混合後之理 包含了第ίβϊΠϊϊΐ之軸向速度在管中對稱_分佈圖， Ζί路對於直管單調的速度分=，=ί S=:L擴、縮效應，造成了流場中形成了大小不-、 切本創作：(⑽上下_形=== 卜⑹_齡⑷。再比匕創 。娜四(e)和柳⑽ 第-段各複製—次並串接喊。分析發現，串接之 議獅—段略㈣，但是在增進 心f三5為直管與本創作各裝置在轴向20倍管徑⑽))處，模 二，方^。由弟二圖之各模擬結果可知，直管型態（a)之混合全賴 屯的擴散效應’其混合之速率相當緩慢，相反的： 水盥藥制、:R i透過在加藥點之後所裝之各種擴縮管，顯著地將污 已速混I待其制下游之直料，_之·度曲線 刀稀>，此說明本創作裝置確實可明顯提升管流之混合功 7 M306894 旎。與本創作一(b)相比，本創作三(c)將擴張角增加，但其混合 成效，顯财如本_三⑷擴張後轉—段大錄再回縮的效果 較本創細⑹與本創作一⑹、本創作五⑴與本創作三⑷ 就可毛現1串聯-隻擴縮管所提升之混合效果仍然可觀。 了進Γ步將混合效應量化，第四0顯示了直管與本創作模 合效率雜向位置之變化鱗，此處混合效率的 Byrde ^ Sawley ^^(Optimization of Kenics static mixer for non-creeping fl〇w conditions, Chemical5 ί=95 sewage is 5. Heart match: J: S ^ L 29 ' 6: s J; think medicine Qi ^ whole (four) words 'plus _ G.43%, (4) after mixing contains the axial speed of the ίβϊΠϊϊΐ In the tube symmetry _ distribution map, Ζί road for the straight tube monotonic speed score =, = ί S =: L expansion and contraction effect, resulting in the formation of the size of the flow field is not -, cut the creation: ((10) up and down _ shape === Bu (6) _ age (4). More than 匕 。. Na four (e) and Liu (10) The first paragraph of each copy - times and shouting shouting. Analysis found that the lion lion - paragraph slightly (four), but in the promotion The heart f 3 is the straight tube and the device of the creation in the axial direction 20 times the diameter (10))), the mold 2, square ^. According to the simulation results of the second diagram, the diffusion effect of the straight tube type (a) is the same as the diffusion effect of the mixture. The rate of mixing is quite slow. On the contrary: the leeches are made, and the R i is transmitted after the dosing point. The various expansion and contraction tubes installed have significantly increased the straightness of the material that has been mixed with the downstream, and the curve of the curve is thin, which means that the creation device can obviously improve the mixing work of the tube flow. Hey. Compared with this creation (b), this creation three (c) increases the expansion angle, but its mixed effect, such as the expansion of the _ three (4) expansion, the effect of the re-retraction of the section of the re-retraction is more than this (6) and this The creation of one (6), the creation of the five (1) and the creation of the third (4) can be achieved by the combination of the 1 series and the expansion tube only. In the step of step, the mixing effect is quantified, and the fourth step shows the scale of the mismatched position of the straight tube and the original model, where the mixing efficiency is Byrde ^ Sawley ^^(Optimization of Kenics static mixer for non-creeping fl 〇w conditions, Chemical
J〇:al ’ V〇1· 72，取 163-169，1999)，為前述理 心〜後之各段藥劑濃度（Q.刪3) ’與 接近1，代表愈接近理想混合結果 ^ Γί ΛΤ^ 合效率作比較，第_巾直管混合的效 作目透獅叙獅対產她速混合的 = 之下祕均可舰合效較酿高則.8以上， ΪΪίίH:本創作各本創作之混合效率曲線在前段擴縮管 中^見巧斜率來說明之。比較本創作個別混合校率，本創作二 管徑處混合效賴為G.85。本創作四和本創作 現Μ 擴^應’故在下游10倍管徑處混合效率曲線出 土弟-波崎率，^它們到達下游25倍管徑處時，Α混合效 均已超過0· 9，其巾本_五之齡鱗更_ 〇 95。 擴縮管職縣奴合產生_⑽益，惟實用上直產生之 楔’第五圖為直管與本創作從加藥點下游 ΪΓ if 線。圖帽示，直管因為流場單純，壓損 //η採之舰設計，#流體流進擴張管時，' 收腿，流場急遽加速，壓力大為下降 ί ίίΓ分接近的本創作二、本創作三與發 張角增大造成的壓損十分顯著，它甚至遠遠超 w 了兩:人擴_本_四和本創作五，姆的，本創作三經由= 8 M306894 伸擴J後f*徑之錢所造成賴損增加卻十分 f張角度相對於混合效率的助益並 ^壓 而言，在歷經25倍管徑長度後，各裝之因素。整體 以下，若換算成水頭高約為衣貝失約在綱議2 無問題。 “刀十刀微小，於實務應用上並 混合之處理流程圖。 α弟七圖為以本創作裝置 ^廠廢水水量為9.4m3/hr，主赌雜 混凝劑為氯化鐵。測試過程中進流水銅Ιίΐί 方式進行齡核，處理後— mg/L(^^ 〇. 33)，97> 83% , =^員不，在相_劑量及水量條件下，改以本創作 二f 雜四）’替代傳統式機械攪拌，進行化學混凝處 ' ==:==(=11.627^ 下，== 』離于降馬U· 127 0· 167 mg/L(平均值〇· 141)，去除率 ^’此處理結果不但略優於傳統式機械游= 低於放流管制標準3mg/L。此—結果說明，以本Ϊ 傳統麟方式，不但可省卻大型赫槽體、獅 ^ 費用，同時也可制職處理功能。 I及動力 M306894 【實施方式】 、^創作裝置應用時之實施方式，可以第七圖為例作說明 一連續肌之流管中，將欲加入之藥劑或特定流體，於本創作元 上游處’以管中加財式由加藥口（12)點注人管流中，使兩 混合並順流而下後，通過本創作裝置，進而產生快速混合作用’ 並在短距離内達到理想的混合效率。 【圖式簡單說明】J〇:al ' V〇1· 72, take 163-169, 1999), for the above-mentioned rationality ~ after the concentration of each agent (Q. delete 3) ' and close to 1, the closer to the ideal mixed result ^ Γί ΛΤ ^Compared with the efficiency, the effect of the _ towel straight tube mixed with the lion lion lion 対 她 她 她 = = = = = = = = = 之下 之下 均可 均可 均可 均可 均可 均可 均可 均可 均可 均可 均可 均可 均可 均可 均可 均可 均可 均可 均可 . . . . . . The mixing efficiency curve is illustrated in the front-end expansion tube. Comparing the individual mixed school rates of this creation, the mixed effect of the second path of this creation is G.85. The creation of the fourth and the present creations is now expanded, and the mixing efficiency curve at the downstream 10 times of the pipe diameter is the same as the Bosaki rate. When they reach the downstream pipe diameter of 25 times, the mixing effect has exceeded 0·9. Its towel _ five ages scales more _ 〇 95. The expansion and contraction of the county's slaves produces _(10) benefits, but the practically produced wedges. The fifth picture shows the straight line and the creation from the downstream of the dosing point ΪΓ if line. The hat shows that the straight pipe is simple because of the flow field, the pressure loss / / η mining ship design, # fluid flow into the expansion tube, 'receive the leg, the flow field is rapidly accelerating, the pressure is greatly reduced ί ίίΓ close to this creation two The pressure loss caused by the creation of the creation three and the increase of the opening angle is very significant. It is even far beyond the w: two people: _ this _ four and the original creation five, m, this creation three via = 8 M306894 The increase in the damage caused by the money of the f* path is quite a factor of the f-angle relative to the benefit of the mixing efficiency, and after the length of the pipe diameter of 25 times, the factors of each load. Overall, if the conversion to the head height is about the loss of the clothes, there is no problem in the outline 2. "The knife is ten small, in the practical application and mixed processing flow chart. The α brother seven map is the waste water volume of this plant is 9.4m3 / hr, the main gambling coagulant is ferric chloride. During the test Influent water copper Ιίΐί way to age nuclear, after treatment - mg / L (^ ^ 〇. 33), 97 > 83%, = ^ staff not, in the phase _ dose and water conditions, change to the creation of two f ) 'Replace the traditional mechanical agitation, chemical coagulation' ======(=11.627^ 下,== 』 从 从 降 降 U U U U U 127 0· 167 mg / L (mean 〇 · 141), remove Rate ^' This treatment result is not only slightly better than the traditional mechanical game = 3mg/L lower than the discharge control standard. This results show that the traditional lining method can not only save the cost of large troughs and lions, but also It can be used to process the functions. I and power M306894 [Embodiment] The implementation method of the application device can be used as an example to illustrate the flow of a drug or a specific fluid to be added to a continuous flow tube. In the upstream of the creation element, the pipe is added to the pipe by the dosing port (12), so that the two mix and flow downstream. After the creation of the present apparatus, thereby generating rapid mixing action 'to achieve the desired mixing efficiency and within a short distance.] [Brief Description of the drawings
第一圖為電腦模擬裝置圖，（a)為未裝置本創作之直管，（b)、 jc)、（d)、（e)、（f)分別為本創作的五種混合裝置。 一圖，電腦模擬之軸向速度分佈圖’（a)為未裝置本創作之直 I ’（b) ' (c)、（d)、（e)、⑴分別為本創作的五種混 己裝置。 第二圖為電腦模擬之藥劑濃度分佈圖，（a)為未裝置本創作之直 ^⑹、⑹，、⑷、⑴分別為本創作的^種混 合裝置。 四圖為電腦模擬之軸向位置混合效率變化曲線圖，圖中”mix … 為混合效率，x(W為沿軸向X倍管徑之距離。 弟五圖為電腦模擬之壓力損變化曲線圖，圖中P為壓力損失 工值’ X(D)為沿軸向X倍管徑之距離。 fA圖為機械混合式處理流程圖。 ^七圖為以本創作裝置混合之處理流程圖。 ί公Ϊ為現場處理後銅離子殘留濃度比較圖。 弟九圖為銅離子去轉比姻。 M306894 【各圖之元件符號簡單說明】 11 12 13 14 15 16 17 601 602 603 604 605 606 607 608 609 610 611 612 71 72 73 74 75 76 77 78 污水管入口 加藥管入口 本創作裝置之一 本創作裝置之二 本創作裝置之三 本創作裝置之四 本創作裝置之五 機械混合式處理流程之污水入口 機械混合式處理流程之pH調整池 機械混合式處理流程之快混池 機械混合式處理流程之慢混池 =械混合式處理流程之沉殿池 =混合式處财程之放流池 混合式處理流程中pH調整池之授拌器 =混合式處理流程中快混池之擾拌器 咄I':合式處理流程中慢混池之擾拌器 pH调整加藥點 混凝劑加藥點 助凝劑加藥點The first picture shows the computer simulation device, (a) is the straight tube without the creation of this creation, and (b), jc), (d), (e), (f) are the five hybrid devices of the creation. In the figure, the axial velocity distribution of the computer simulation '(a) is the original I '(b) ' (c), (d), (e), (1) of the original creation of the five kinds of mixed creation Device. The second picture shows the concentration distribution of the drug in the computer simulation, and (a) is the mixing device that is not created by the original (^), (6), (4), and (1). The four figures are the simulation results of the axial position mixing efficiency of the computer simulation. In the figure, “mix ... is the mixing efficiency, x (W is the distance of the X-tube diameter along the axial direction.) The fifth figure is the pressure loss curve of the computer simulation. In the figure, P is the pressure loss value 'X(D) is the distance X along the axial direction. The fA diagram is the mechanical hybrid processing flow chart. ^The seven diagram is the processing flow chart mixed by the authoring device. The gong is the comparison of the residual concentration of copper ions after on-site treatment. The figure of the nine is the copper ion to turn the ratio. M306894 [Simple description of the symbol of each figure] 11 12 13 14 15 16 17 601 602 603 604 605 606 607 608 609 610 611 612 71 72 73 74 75 76 77 78 Sewage pipe inlet medicated pipe inlet One of the authoring devices of the author of the author of the author of the creation of the four creative devices of the four creative devices of the five mechanical mixing process sewage The pH adjustment pool of the inlet mechanical mixing process, the mechanical mixing process, the fast mixing pool, the mechanical mixing process, the slow mixing pool, the mechanical mixing process, the sinking pool, the hybrid, the fiscal process, the mixing pool, the mixing process. Process pH was adjusted pools grant stirrer = hybrid process flow speed mixing pools scrambler stirrer duh I ': fit process flow slowly mixed pools scrambler stirrer pH adjusted dosing point coagulant dosing point coagulant dosing point
Sit裝置處理流程之污水入口 使用本創作梦番:瓜你〜叫网㈣ 使用本創理流程之本創作裂置 使用本創作理流程之助凝劑加 凌置處理流程之慢混池攪拌器 凝劑加藥點 使用太凌:1裝置處理流程之慢混池 #用U作裝置處理流程之沉殿池 =:裝置處理流程之放流池 传田^裴置處理流程之pH調整與助 藥點 11The sewage inlet of the Sit device processing process uses this creation dream fan: melon you ~ called the net (four) using this creative process of the creation of the use of the creative process of the coagulant plus the processing of the slow mixing pool mixer condensation The dosage point of the dosing agent is Tailing: 1 The slow mixing pool of the processing flow of the device # The sinking pool of the processing flow of the U device is used: the discharge tank of the device processing flow, the pH adjustment and the dosing point of the treatment process