M311475 八、新型說明： ， 【新型所屬之技術領域】 本創作為一種混絮凝裝置，係可廣泛使用在磁聚分離裝置、 >儿;展又1置、浮除裝置、過濾裝置之前置，作為加藥混合、物理強 化處理及混絮難狀魏，_是在該慢混絮凝裝置之筒體外 部繞设加藥混凝裝置，而構成整合性的機構，致可確實縮小混絮 凝反應的構造體積，並可縮小佔用空間及降低投資成本，據此達 φ 到增進經濟效益之原則，暨有效提昇其產業之利用價值者。 【先前技術】 按，一般習知之混凝構造，係採用機械式單槽高速攪拌，在 混凝劑局部集中的位置使污泥雜詩花將快速長大，致形成鬆散 的磐花顆粒，當遇到較強的剪切力其吸附橋則會被剪斷，而產生 局部過度反應現象；另外，在該藥劑未擴散之處其膠體顆粒尚未 脫穩’此部份絮凝反應勢必不夠完善。以上習用結構基本上主要 • 照顧了巨觀擴散，卻忽略了微觀擴散作用。 再者’另一習用的絮凝構造，係以隔板方式來改變流速及速 度梯度’故僅於轉彎處才有有效G值，其缺點為直線區域的作用 不大，且其慢速區會有沉;殿及積留的困擾。 【新型内容】 t斯此’本案二創作人乃執創新精神，著手索思構設，秉多 年從事環境保墁工程、過濾桶槽、曝氣機及各種產品之創作、設 计的經驗積極研發，且在多方條件的審慎參酌下，擷取各種結構 M311475 ’俾可解決 的得失利弊考量，終於開發出本創作『混絮凝裝置』 習用之困擾。 亦即，本創作之主要目的乃在於提供_種混絮凝裝置，其係 於該慢混絮凝裝置之筒體外部繞設加藥混凝裝置，而形成敕人糸 的結構，致能確實縮小混絮凝反應的構造材積，更由於 σ 的ΡΗ調整池及混絮凝池等一系列大型設備，並可節省佔用空間及M311475 VIII. New description: , [New technical field] This creation is a kind of mixing flocculation device, which can be widely used in magnetic polymerization separation device, >children; exhibition and 1 set, floating device, filter device before setting As a dosing mixing, physical strengthening treatment and mixing of fluffy Wei, _ is to set up a drug-adding coagulation device outside the cylinder of the slow-mixing flocculation device, and constitute an integrated mechanism, so as to narrow the mixed flocculation reaction The construction volume can reduce the occupied space and reduce the investment cost, and accordingly, the principle of increasing economic benefits and improving the utilization value of the industry. [Prior Art] According to the conventionally known coagulation structure, the mechanical single-slot high-speed agitation is used, and the localized concentration of the coagulant will cause the sludge to grow rapidly, resulting in the formation of loose squid particles. Strong shear force will cause the adsorption bridge to be sheared, resulting in local over-reaction; in addition, the colloidal particles have not destabilized where the agent has not diffused'. This part of the flocculation reaction is bound to be insufficient. The above-mentioned conventional structure is basically the main • taking care of the macroscopic diffusion, but neglecting the microscopic diffusion. Furthermore, 'another conventional flocculation structure is to change the flow velocity and velocity gradient by means of a diaphragm.' Therefore, there is an effective G value only at the turn, and the disadvantage is that the linear region has little effect, and the slow region has Shen; the temple and the accumulation of trouble. [New Content] t Si's creator of this case is an innovative spirit, set out to design, and has been actively engaged in research and development of environmental protection projects, filter tanks, aerators and various products. Under the discretion of various conditions, we have taken into consideration the various advantages and disadvantages of the various structures M311475's, and finally developed the habit of using the "mixed flocculation device". That is to say, the main purpose of the present invention is to provide a hybrid flocculation device which is arranged on the outside of the cylinder of the slow-mixing flocculation device to form a compounding and coagulating device, thereby forming a structure of a human being, which enables the actual mixing and reduction. The structural volume of the flocculation reaction is more due to a series of large-scale equipment such as σ ΡΗ adjustment pool and mixing flocculation tank, and can save space and
降低投貢成本，達致增進經濟效益之原則，有效提昇其產業 用價值者。 、，、之利 【實施方式】 為使貴審查委員能進一步瞭解本創作之結構特徵及實用功 效，茲以下文所述之較佳實施例配合圖式詳細說明如后： 首S’請參閱第-圖和第二圖所示，本創作實施例所提供係 為一種混絮凝裝置，主要包括加藥混凝裝置（1〇)以及慢混絮凝穿 置（20)等構件，促使玉業㈣磨廢水和各種污水能細行細顆粒 翁義磁;!㈣，以及適當的藥觀合絮凝分離成為料的水及 污泥雜質顆粒，其中； 該加藥混凝裝置（10)概呈中空螺旋輸導軟管（11)狀，係在該 進水口（111)附近套設有具磁性之預磁器（⑵，乃於其管段間距的 適當處裝置有數組取樣口（131)及加藥口一（132)、加藥口二（133) 以及預混器（14)，而該預混器（14)係可快速地讓污水和各種藥劑 進行巨觀混合、反應，上述整體該加藥混凝裝置（1〇)係組裝環繞 設在k混絮凝裝置（20)的外周，其係藉由末端轉流口（丨12)與慢混 M311475 絮凝裝置（20)之筒體（21)連接相通； 再請配合參閱第一圖、第三圖和第四圖所示，該慢混絮凝裝 置（20)係在密閉筒體（21)内部利用數根組立柱（221)和多數套管 (222)間隔疊組小隔板(23)和大隔板（24)，以使每一片小隔板(23) 和母一片大隔板（24)之間預留有間隔空間（25)’其間係以中隔板 (26)分隔成流入部（31)與流出部（32)，係在該小隔板(23)外周預 留有外側空間（231)，而於大隔板（24)内部預留有内側空間 (241)，乃於該筒體(21)頂面開設入水口（211)，俾與該加藥混凝 裝置（10)之轉流口（112)相接互通，至於該出水口（212)則係由輸 導軟管（11)連通至磁分離裝置（40)或後續分離裝置，且在該出水 口 (212) —旁開設取樣口（213)。 上述本創作該中隔板（26)係得視處理污水不同種類的需求 而作增加或減少，亦即分割流入部⑶）與流出部（32)的多募而俾 令污水慢混絮凝之過程合乎最適當的需要。 " 以上所述即林_混絮凝裝置，其之各組件_構造及位 置之概述。 •優點能有更進一步 本創作遇絮凝裝置所能職達成之功效陳述如 后’期使β查委s先生對袖作之特徵及 之體會與認識。 再請配合參看第二圖所示，本: 凝裝置（10)輸導軟管（11)之進水口 力污水，以使污水通過預磁 ⑽所述構造係得從該加藥混 σ (111)導入經過幫浦加壓之壓 (12)而令其磁場對水中之磁性顆粒 M311475 _物作磁性助敎，俾增強水中磁性顆粒物的凝聚力和磁場的作用 ~ 力❿使3在水中的雜質在強力磁場的作用下發生擠壓和快速凝 *作用Μ而在雜樣口（131)錄污水測試污水的性質，其係得 於各道加藥口一（132)及加藥口二（133)各別加入例如·· ρΗ調節 劑、混絮凝劑和磁種助凝劑、或其他藥劑、並溶人氣體，再讓污 水中的雜質以_形態分離出來，絮;疑混合形成微絮凝團，繼續 攸趟導軟官（⑴往後流送，再次於另一取樣口（⑶）截取混合絮 • 凝後之污水測試性質，而於另一加藥口一（132)、加藥口二（133) 各別裝置例如：紫外光照射、超聲波照射、微波輻射，以強化絮 凝混合後該污水的化學反應，再次讓污水中的雜質絮凝混合形成 微絮凝團，分離後之水則繼續從該輸導軟管（11)往後流動，最後 將該加藥混絮凝過後之污水透過轉流口（112)，繼續從該筒體(21) 之入水口（211)導進慢混絮凝裝置（2〇)之中，進行下一段的慢混絮 凝過程。 Φ 繼如第五圖及第一圖所示，上述加入各種化學藥劑混絮凝處 理過後之污水係從慢混絮凝裝置（20)筒體（21)之入水口（211)導 入’輾轉環繞從流入部（31)小隔板（23)之外側空間（231)轉流經過 間隔空間（25) ’再從該大隔板（24)之内側空間（241)這樣輾轉環繞 逐漸往下流，再導流通過該流出部（32)之小隔板（23)外側空間 (231)輾轉環繞流經過該大隔板（24)之内側空間（241)如此輾轉環 繞逐漸往上流，據上持續環繞的流動並不斷改變污水及雜質的流 速和方向，並使顆粒一個抓一個的逐漸凝聚長大，繼從該筒體（21) M311475 之出水口（212)流進磁分離裝 淨水的分離輸出。 置(40)或後續分離裝置進行雜 質和 總結以上說明，可知本創作『混絮凝裝置』 空間型態，不僅是-個整合性的縮小結構，確實—掃昔知= 之 且使其整個混絮凝反應的構積能夠比賴小，/， 之效益，有效提昇其產業之湘價值 ,μ羥濟 優显、突出之創斩…+ ’誠不失為— 出之_s又计，且經實物樣品證實確實可達成預期之目 的，應合科概新奴各項將，纽缺請糊。目 【圖式簡單說明】 第一圖係本創作一種實施例組合立體圖。 第二圖係本創作之組合立體圖。 第三圖係本創作慢混絮凝裝置之立體透視圖。 第四圖係本_慢混絮凝裝置内部之構造組合立體圖。 第五圖係本創作慢混絮凝裝置之污水和雜質的流向示意圖。 【主要元件符號說明】 (10) 加藥混凝裝置 (112)轉流口 (133)加藥口二 (212)出水口 (11) 輸導軟管 （111)進水口 (12) 預磁器 (131)取樣口 （132)加藥口 (14)預混器 (20) 慢混絮凝裝置 (21) 筒體 （211)入水口 M311475 (213)取樣口 (221)組立柱 (222)套管 (23)小隔板 (231)外側空間 (24) 大隔板 (25) 間隔空間 (26) 中隔板 (31) 流入部 (32) 流出部 (40)磁分離裝置 (241)内側空間 ΙΟReduce the cost of tribute, achieve the principle of improving economic efficiency, and effectively improve the value of its industrial use. Benefits, Implementations, etc. [In order to enable the review committee to further understand the structural features and practical functions of the creation, the preferred embodiments described below are described in detail with the drawings as follows: First S' please refer to - shown in the figure and the second figure, the present embodiment provides a mixing flocculation device, which mainly comprises a medicinal coagulation device (1 〇) and a slow mixing flocculation through (20) member, and promotes the jade industry (four) grinding. Waste water and various sewages can finely granulate Wengyi magnetic; (4), and appropriate drug flocculation and separation into water and sludge impurity particles, wherein the dosing coagulation device (10) is hollow spiral The guide hose (11) is provided with a magnetic pre-magnetic device ((2) near the water inlet (111), and an array sampling port (131) and a dosing port are provided at appropriate intervals of the pipe spacing ( 132), dosing port 2 (133) and premixer (14), and the premixer (14) can rapidly mix and react sewage and various chemicals, and the above-mentioned whole dosing and coagulation device (1〇) is assembled around the outer circumference of the k-flocculation flocculation device (20) The end transfer port (丨12) is connected to the barrel (21) of the slow mixing M311475 flocculation device (20); please refer to the first, third and fourth figures together with the slow mixing flocculation device. (20) A plurality of small partitions (23) and large partitions (24) are stacked inside the closed cylinder (21) by using a plurality of sets of columns (221) and a plurality of sleeves (222) so that each piece is separated A space (25) is reserved between the plate (23) and the female large partition (24). The middle partition (26) is partitioned into an inflow portion (31) and an outflow portion (32). An outer space (231) is reserved in the outer periphery of the small partition plate (23), and an inner space (241) is reserved inside the large partition plate (24) to open the water inlet (211) on the top surface of the cylindrical body (21). , the 俾 is in communication with the diversion port (112) of the dosing coagulation device (10), and the water outlet (212) is connected to the magnetic separation device (40) or the subsequent by the transfer hose (11) Separating device, and opening a sampling port (213) next to the water outlet (212). The above-mentioned partition (26) is increased or decreased according to the different types of sewage treatment requirements, that is, the divided inflow portion (3)) The outflow section (32) and serve multiple raised flocculation of sewage water mixed slowly during the most desirable appropriate needed. " The above is a summary of the components and structures of the forest-mixed flocculation device. • Advantages can be further improved The performance of the creation of the flocculation device can be achieved as stated in the following paragraphs, so that the characteristics of the sleeves and the understanding and understanding of the sleeves. Please refer to the second figure again. This: The condensing device (10) transports the inlet pipe of the hose (11) to make the sewage pass through the structure of the pre-magnetism (10). Introduce the pressure (12) of the pressurized pressure of the pump to magnetically assist the magnetic particles M311475 in the water, and enhance the cohesive force and magnetic field of the magnetic particles in the water. Extrusion and rapid condensation under the action of a strong magnetic field, and the nature of the sewage test in the sample mouth (131), which is obtained from each of the dosing ports (132) and the dosing port two (133) Each of them is added, for example, a ρΗ adjusting agent, a flocculating agent and a magnetic coagulant, or other chemicals, and a human gas is dissolved, and the impurities in the sewage are separated in a _ form, and the flocculation is mixed to form a microflocculation group. Continue to guide the soft official ((1) to send backwards, again at another sampling port ((3)) to intercept the nature of the mixed flocculation and condensed sewage test, and in another dosing port one (132), dosing port two ( 133) Individual devices such as: ultraviolet light, ultrasonic radiation, microwave radiation to enhance the floc After the mixing, the chemical reaction of the sewage again causes the impurities in the sewage to flocculate and form a micro-flocculation group, and the separated water continues to flow backward from the conveying hose (11), and finally the sewage after the mixing and flocculation Through the diversion port (112), continue to introduce the slow mixing flocculation device (2〇) from the water inlet (211) of the cylinder (21) into the slow mixing flocculation process of the next section. Φ Follow the fifth figure As shown in the first figure, the sewage system after the above-mentioned various chemical agents are mixed and flocculated, and introduced into the water inlet (211) of the cylinder (21) of the slow-mixing flocculation device (20), which is surrounded by the inflow portion (31). The outer space (231) of the plate (23) is diverted through the space (25) and is further circulated downward from the inner space (241) of the large partition (24), and then flows through the outflow (32). The outer space (231) of the small partition (23) wraps around the inner space (241) of the large partition (24) so as to be circulated and gradually flows upward, and continues to surround the flow and continuously change the sewage and impurities. Flow rate and direction, and gradually condense the particles one by one Large, following the separation output from the water outlet (212) of the cylinder (21) M311475 into the magnetic separation water. Placement (40) or subsequent separation device for impurities and summarizing the above description, we can see that the creation of the "coagulation flocculation device" The spatial pattern is not only an integrated and reduced structure, but also the structure of the whole mixed flocculation reaction can be compared with the small, /, effective, and effectively enhance the value of its industry.羟 羟 优 优 、 突出 + + + + + + + + + + + + + + + + + + + + + + + + + + + + + + + + + + + + + + + + + + + + + + [Simplified description of the drawings] The first figure is a combined perspective view of an embodiment of the present invention. The second picture is a combined perspective view of the creation. The third figure is a perspective view of the slow mixing flocculation device of the present invention. The fourth figure is a perspective view of the construction of the interior of the _ slow mixing flocculation device. The fifth figure is a schematic diagram of the flow direction of sewage and impurities of the present slow mixing flocculation device. [Description of main component symbols] (10) Dosing coagulation device (112) diversion port (133) dosing port two (212) water outlet (11) Conveying hose (111) water inlet (12) Pre-magnetic device ( 131) sampling port (132) dosing port (14) premixer (20) slow mixing flocculation device (21) cylinder (211) inlet M311475 (213) sampling port (221) group column (222) casing ( 23) Small partition (231) Outside space (24) Large partition (25) Space (26) Middle partition (31) Inflow (32) Outflow (40) Magnetic separation device (241) Inside spaceΙΟ