JP4742338B2 - Mixing device and method for treating polluted water using the mixing device - Google Patents

Mixing device and method for treating polluted water using the mixing device Download PDF

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JP4742338B2
JP4742338B2 JP2005095981A JP2005095981A JP4742338B2 JP 4742338 B2 JP4742338 B2 JP 4742338B2 JP 2005095981 A JP2005095981 A JP 2005095981A JP 2005095981 A JP2005095981 A JP 2005095981A JP 4742338 B2 JP4742338 B2 JP 4742338B2
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supply hopper
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倫 波多野
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日本ソリッド株式会社
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Description

本発明は、液体、粉体等の混合物質を流体と混合するための混合装置およびその混合装置を用いた汚濁水の処理方法に関する。  The present invention relates to a mixing apparatus for mixing a mixed substance such as liquid or powder with a fluid and a method for treating contaminated water using the mixing apparatus.

従来、特に水等の液体に溶解し難い難溶性の混合物質を溶解する装置として、例えば被溶解物質の供給ホッパーの下端に取外し自在に装着され且つその内部軸方向に被溶解物質を通過させるための中央通路を有する本体と、前記本体を部分的に収納する内部室およびこの内部室に連通して軸方向に伸び前記被溶解物質を通過させるための落下通路を有するハウジングとからなり、前記被溶解物質を溶解するための溶媒を前記ハウジングの側壁を通して前記内部室の前記本体との間に形成される環状空間に導いて落下せしめ前記中央通路を通過して落下する被溶解物質と合流混合して溶解する溶解装置において、前記本体の下部には前記中央通路を形成する環状内壁と、前記環状内壁の外側に同心的にエアカーテン形成用環状空間を残して環状外壁とを形成し、前記エアカーテン形成用環状空間は本体の軸方向に伸びる複数個の管路を介して大気と連結している、溶解装置が知られている(特許文献1参照)。  Conventionally, as a device for dissolving a hardly soluble mixed substance that is difficult to dissolve in a liquid such as water, for example, it is detachably attached to the lower end of a supply hopper of the dissolved substance and allows the dissolved substance to pass in the direction of the inner axis thereof. A main body having a central passage, a housing having a chamber for partially containing the main body, and a housing having a dropping passage for communicating with the inner chamber and extending in the axial direction to pass the substance to be dissolved. A solvent for dissolving the dissolved substance is guided through the side wall of the housing to the annular space formed between the main body of the inner chamber and dropped to join the dissolved substance falling through the central passage. In the melting apparatus for melting, an annular inner wall forming the central passage is formed in the lower portion of the main body, and an annular space is formed concentrically on the outer side of the annular inner wall, leaving an annular space for forming an air curtain. Forming a wall, the air curtain forming annular space is connected to the atmosphere via a plurality of conduits extending in the axial direction of the main body, dissolving device is known (see Patent Document 1).

特許文献1 実公昭50−34288号公報  Patent Document 1 Japanese Utility Model Publication No. 50-34288

前記した溶解装置は、被溶解物質を溶解するためには満足し得るものではある品点数が多いために解体、組立に時間を要し、装置が高価になるという欠点があった。
そこで本発明は、混合物質を流体と均一に混合でき、装置の部品点数も少なく、解体、組立が容易で、かつ混合した後の流体をマイナスイオン化(酸化還元電位が低い)させることのできる混合装置について種々検討した結果本発明を完成するに至った。
Wherein the dissolution apparatus is to dissolve the dissolvable material is intended satisfactory, disassembled because many number of parts, takes time to assemble, has a drawback that the apparatus becomes expensive.
Therefore, the present invention can mix the mixed substance uniformly with the fluid, the number of parts of the apparatus is small, disassembly and assembly are easy, and the mixed fluid can be negatively ionized (low oxidation-reduction potential). As a result of various studies on the apparatus, the present invention has been completed.

すなわち、本発明は、供給ホッパーと、内部軸方向に中央通路を有する本体と、前記本体を収納する内部室を有するハウジングからなり、混合物質と混合するための流体を前記ハウジングの側壁を通して前記内部室と前記本体との間に環状空間が形成されるように設けて、前記中央通路部を通過して落下する混合物質と流体とを合流混合させる混合装置において、前記供給ホッパーの排出管を前記本体の中央通路に挿入し、その供給ホッパーの排出口に、少なくとも上部に棒状体を垂直に設けた震動弁を設け、ハウジングの内部室の壁面に湾曲した凹み部を設け、前記本体の外壁面に垂直状あるいは斜線状の溝を設けたことを特徴とする混合装置である。  That is, the present invention comprises a supply hopper, a main body having a central passage in the inner axial direction, and a housing having an inner chamber for accommodating the main body, and a fluid for mixing with a mixed substance passes through the side wall of the housing through the inner wall. In a mixing device that is provided so that an annular space is formed between a chamber and the main body, and mixes and mixes the mixed substance and fluid that fall through the central passage portion, the discharge pipe of the supply hopper includes the discharge pipe Inserted into the central passage of the main body, provided at the discharge port of the supply hopper with a vibration valve provided with a rod-like body vertically at least at the top, provided with a curved recess in the wall surface of the inner chamber of the housing, This is a mixing device characterized in that a vertical or oblique groove is provided in the.

本発明の混合装置は、部品点数が少なく、かつ解体、組立が容易で、また解体、組立の頻度を少なくすることができ、混合物質と流体を混合するだけでなく、溶解或いは分散させ、さらに混合した後の流体をマイナスイオン化することができる。  The mixing device of the present invention has a small number of parts, is easy to disassemble and assemble, and can reduce the frequency of disassembling and assembling. The fluid after mixing can be negatively ionized.

次に本発明を図面を参照しながら説明するが、本発明は、以下の説明のみに限定されるものではない。
図1は、本発明の混合装置の断面図である。
1は、供給ホッパーすなわち液体、粉体等の混合物質の受槽で、供給ホッパー1の排出口2には下部に排出管3が設けられている。この供給ホッパー1の排出口2には図2に示す震動弁4が設けられている。
Next, the present invention will be described with reference to the drawings, but the present invention is not limited to the following description.
FIG. 1 is a cross-sectional view of the mixing apparatus of the present invention.
Reference numeral 1 denotes a supply hopper, that is, a receiving tank for a mixed substance such as liquid or powder. A discharge pipe 3 is provided at the lower portion of the discharge port 2 of the supply hopper 1. The discharge port 2 of the supply hopper 1 is provided with a vibration valve 4 shown in FIG.

この震動弁4は、球形又は紡重形、楕円形等の弁本体5に、少なくとも上部に棒状体6を一体に設ける。また弁本体5の表面全体に突起状物を設けることによって、粉末状の混合物質を供給するときに排出口2にブリッジを形成するのを防止することができる。棒状体6の形状は、直線状であっても螺線状であっても良い。また棒状体6の形状は横断面形状が丸形、三角形、四角形、楕円形等の種々の形状のものが使用でき、これらの棒状体6は中空体であってもよい。  This vibration valve 4 is integrally provided with a rod-like body 6 at least at an upper part of a valve body 5 having a spherical shape, a spinning shape, an elliptical shape or the like. Further, by providing a protrusion on the entire surface of the valve body 5, it is possible to prevent a bridge from being formed in the discharge port 2 when supplying the powdery mixed substance. The shape of the rod-like body 6 may be linear or spiral. The rod-shaped body 6 may have various cross-sectional shapes such as a round shape, a triangular shape, a quadrangular shape, an elliptical shape, and the like. The rod-shaped body 6 may be a hollow body.

球形又は紡重形、楕円形等の弁本体5は、内部に偏心プーリーを設けた小型モーターを内蔵させることによって震動弁4を躍動させることができる。小型モーターを駆動する電源は、弁本体5内に電池等を内蔵するか、中空棒状体6の中空部内にも電線を配して外部より取ることもできる。  The valve body 5 having a spherical shape, a spinning shape, or an elliptical shape can vibrate the vibration valve 4 by incorporating a small motor having an eccentric pulley therein. The power source for driving the small motor can be taken from the outside by incorporating a battery or the like in the valve body 5 or by arranging an electric wire in the hollow portion of the hollow rod-like body 6.

図3は、本発明の混合装置の本体側面図である。
7は、本体であり、本体7には内部軸方向に中央通路8を有している。本体7の中央通路8を構成する環状円筒体9の外壁面には、図3に示すように直線状あるいは非直線状あるいは非直線状と直線状の組み合わされた溝10を設けることが好ましい。そして非直線状と直線状の組み合わされた溝の場合、後述する、本体7の円筒体9とハウジング14の内部室12との間に形成される環状空間13を流体が流れる方向と逆に非直線状にして設けることにより均一流とすることができるので、好ましい。
FIG. 3 is a side view of the main body of the mixing apparatus of the present invention.
Reference numeral 7 denotes a main body, and the main body 7 has a central passage 8 in the inner axial direction. On the outer wall surface of the annular cylindrical body 9 constituting the central passage 8 of the main body 7, it is preferable to provide a groove 10 that is linear, non-linear, or a combination of non-linear and linear as shown in FIG. In the case of a groove combined with a non-linear shape and a linear shape, a non-reversal direction in which the fluid flows in an annular space 13 formed between the cylindrical body 9 of the main body 7 and the inner chamber 12 of the housing 14, which will be described later. Since a uniform flow can be obtained by providing a straight line, it is preferable.

図4は、本発明の混合装置のハウジングの断面図である。
本体7を収納する内部室12を有するハウジング14には、その内部室12の壁面に環状の湾曲した形状の凹み部又は直線の間隙15を設けてある。また、ハウジング14には、その内部室12に流体を導入するための流体源に通じている接続管16が設けられて、内部室12の環状空間13に開口しており、その流入口17の軸線は内部室12の中心軸線に偏倚している。
FIG. 4 is a cross-sectional view of the housing of the mixing device of the present invention.
A housing 14 having an internal chamber 12 that accommodates the main body 7 is provided with an annular curved recess or a straight gap 15 on the wall surface of the internal chamber 12. The housing 14 is provided with a connecting pipe 16 that leads to a fluid source for introducing fluid into the internal chamber 12, and opens to the annular space 13 of the internal chamber 12. The axis is biased to the central axis of the internal chamber 12.

本発明の混合装置は、ハウジング14の内部室12に本体7の環状円筒体9を挿入し、例えば図1に示すようにボルト18によって一体に構成する。このように構成することにより、内部室12と、本体7の環状円筒体9との間に環状空間13が形成される。  In the mixing apparatus of the present invention, the annular cylindrical body 9 of the main body 7 is inserted into the inner chamber 12 of the housing 14 and is integrally formed by bolts 18 as shown in FIG. With this configuration, an annular space 13 is formed between the inner chamber 12 and the annular cylindrical body 9 of the main body 7.

この環状空間13の形状としては、湾曲形状の半円形等、角形状の四角・三角等の多角形状が挙げられる。中でも頂角が120°の三角形状が好ましく、流体のエネルギーを減少させること無く溝10へ通すことが出来る。  Examples of the shape of the annular space 13 include a polygonal shape such as a square shape and a triangular shape such as a curved semicircle. In particular, a triangular shape having an apex angle of 120 ° is preferable, and the apex angle can be passed through the groove 10 without reducing fluid energy.

次に、本体7の中央通路8に供給ホッパー1の排出管3を挿入する。供給ホッパー1の固定は、例えば本体7と供給ホッパー1の排出管3とを螺合等することによって行うことができる。排出管3の長さは、供給ホッパー1を挿入したときに排出管3の先端部が本体7の中央通路8の先端部との面と同一となるか、中央通路8の先端部面より突出するように調整することが好ましい。尚、本体7の中央通路8に供給ホッパー1の排出管3を挿入する構造で、中央通路8と排出管3は絶縁され、被溶解物質が本体に付着しないので、排出管3を取り外すだけの簡単な清掃で済む。  Next, the discharge pipe 3 of the supply hopper 1 is inserted into the central passage 8 of the main body 7. The supply hopper 1 can be fixed by, for example, screwing the main body 7 and the discharge pipe 3 of the supply hopper 1 together. The length of the discharge pipe 3 is the same as that of the front end portion of the central passage 8 of the main body 7 when the supply hopper 1 is inserted or protrudes from the front end surface of the central passage 8. It is preferable to adjust so as to. The discharge pipe 3 of the supply hopper 1 is inserted into the central passage 8 of the main body 7. The central passage 8 and the discharge pipe 3 are insulated and the substance to be dissolved does not adhere to the main body. Easy cleaning.

供給ホッパー1の排出管3の口径を調整するためには、供給ホッパー1内に供給ホッパー1と同型の小型化したホッパーを排出口2に設けることによって可能である(図示せず)。  In order to adjust the diameter of the discharge pipe 3 of the supply hopper 1, it is possible to provide a small hopper of the same type as the supply hopper 1 in the supply hopper 1 at the discharge port 2 (not shown).

次に本発明の混合装置を用いて粒体・粉体(CMC、高分子凝集剤、活性炭等)等を水と混合する場合について説明する。
震動弁4を停止させて、粉体を供給ホッパー1内に入れ貯留し、震動弁4を作動させると、震動弁4は震動しながら跳動回動運動を行う。震動弁4の跳動回動運動に伴い、震動弁4に設けられた上部の棒状体6が供給ホッパー1の壁面に伴うように跳動回動するため、供給ホッパー1内の粉体の供給ホッパー1内でのブリッジを防止することができる。また震動弁4に設けられた下部の棒状体6は排出口2内を回動することによって、粉体が排出管3内での閉塞を防止することができる。震動弁4は粉体の弁機能・ブリッジ防止機能の他に粉体の微調節、定量注入等の多様な機能を有するものである。
Next, a case where particles / powder (CMC, polymer flocculant, activated carbon, etc.) and the like are mixed with water using the mixing apparatus of the present invention will be described.
When the vibration valve 4 is stopped and the powder is placed in the supply hopper 1 and stored, and the vibration valve 4 is operated, the vibration valve 4 performs a jumping and pivoting motion while vibrating. Along with the jumping and turning movement of the vibration valve 4, the upper rod-like body 6 provided on the vibration valve 4 jumps and turns so as to follow the wall surface of the supply hopper 1, so that the powder supply hopper 1 in the supply hopper 1. Bridging inside can be prevented. Further, the lower rod-like body 6 provided in the vibration valve 4 rotates in the discharge port 2 so that the powder can be prevented from being blocked in the discharge pipe 3. The vibration valve 4 has various functions such as fine adjustment of powder and quantitative injection in addition to the powder valve function and bridge prevention function.

震動弁4は、供給ホッパー1の排出口2を閉鎖する弁体と震動駆動部が一体となり、オフの状態で弁本体5は重力弁(ゴム・金属、合成樹脂、セラミック・紙材製など)として閉まり、電動、電磁気操作等の震動により震動弁4が上下に振動し、左右に回転して跳動運動する事によって、ホッパー1の排出口2や排出管3および被溶解物質等に震動を与え、震動弁4がオン・オフを繰り返しながら、ブリッジや閉塞が起きない装置である。  The vibration valve 4 is a valve body that closes the discharge port 2 of the supply hopper 1 and a vibration drive unit, and the valve body 5 is a gravity valve (rubber / metal, synthetic resin, ceramic / paper, etc.) in the off state. The vibration valve 4 vibrates up and down due to vibrations such as electric and electromagnetic operations, and jumps by rotating left and right to give vibration to the discharge port 2 and the discharge pipe 3 of the hopper 1 and the substance to be dissolved. In this device, the vibration valve 4 is repeatedly turned on and off, so that no bridge or blockage occurs.

図5は、本発明の混合装置の震動弁4の1実施態様を示す断面図である。
供給ホッパーから混合物質の落下量を調整するためには、棒状体の長さを調整し、その棒状体6の先端部を供給ホッパー上縁部を供給ホッパー上縁部11に適当な手段で掛り止めすることによっておこなうことができる。
FIG. 5 is a cross-sectional view showing one embodiment of the vibration valve 4 of the mixing apparatus of the present invention.
In order to adjust the amount of the mixed substance falling from the supply hopper, the length of the rod-shaped body is adjusted, and the tip of the rod-shaped body 6 is hooked on the upper edge of the supply hopper by an appropriate means on the upper edge 11 of the supply hopper. It can be done by stopping.

一方ハウジング14に設けられた接続管16から、内部室12と本体7によって形成された環状空間13に流体(液体・気体等)が導入されると、流体は環状空間13内を旋回するように流れる。この時ハウジング14の内部室12に設けられた環状の湾曲した形状の凹み部15があることから、旋回が早くなると共に環状空間13内の圧力を高めることができる。流体はこの環状空間13内から本体7の直線状あるいは非直線状あるいは非直線状と直線状の組み合わされた溝10を通り外部に高圧噴出されると流体が交差衝突し、マイナスイオン化現象が生じる。  On the other hand, when fluid (liquid, gas, etc.) is introduced from the connecting pipe 16 provided in the housing 14 into the annular space 13 formed by the inner chamber 12 and the main body 7, the fluid swirls in the annular space 13. Flowing. At this time, since there is an annular curved recess 15 provided in the inner chamber 12 of the housing 14, the turning speed is increased and the pressure in the annular space 13 can be increased. When fluid is ejected from the annular space 13 through the linear, non-linear, or non-linear and linear grooves 10 of the main body 7 to the outside, the fluid intersects and a negative ionization phenomenon occurs. .

この噴出された流体と供給ホッパー1の排出管3から落下した粉体はハウジング14の出口部において一瞬にして混合され混合装置外に排出される。  The jetted fluid and the powder falling from the discharge pipe 3 of the supply hopper 1 are mixed instantaneously at the outlet of the housing 14 and discharged out of the mixing apparatus.

流体エネルギーを環状空間13と凹み部15があることから旋回流で加速、加圧し円周上の前方位に切削された本体7の直線状あるいは非直線状あるいは非直線状と直線状の組み合わされた溝10から下部中央に流体が噴流し集中で交差して、強い衝突エネルギーを持つ高圧ジェット流と成る。ホッパー1の排出口2から排出管3を経由して、機器本体中央部から落下する粉体・液体等の被溶解物質が前述の高圧ジェット流により、空中間で瞬間的に溶解、混合、攪拌などが行われる。なお高圧ジェット流により細粒化された流体は、マイナスイオン化し、溶解物質の鮮度保持並びに添加混合物質の電気・化学反応、物理的等の多様効果を得ることができる。  Since there is an annular space 13 and a dent 15 in the fluid energy, the body 7 that is accelerated and pressurized by a swirling flow and cut in the forward direction on the circumference is linear, non-linear, or a combination of non-linear and linear. The fluid jets from the groove 10 to the center of the lower part and intersects in a concentrated manner to form a high-pressure jet stream having strong collision energy. Substances to be dissolved such as powder and liquid falling from the central part of the device main body through the discharge pipe 3 from the discharge port 2 of the hopper 1 are instantaneously dissolved, mixed and stirred in the air by the high-pressure jet flow described above. Etc. are performed. The fluid finely divided by the high-pressure jet flow is negatively ionized, and various effects such as maintaining the freshness of the dissolved substance and the electric / chemical reaction and physical properties of the added mixed substance can be obtained.

被溶解物質は、高圧ジェット流と成った流体の中心部に落下させると、瞬間圧力で捻じ込まれ、難溶解性の粉末においても、空中間で混合・溶解され、ママコ状態にならない。  When the substance to be dissolved is dropped into the center of the fluid formed as a high-pressure jet stream, it is screwed in by instantaneous pressure, and even a hardly soluble powder is mixed / dissolved in the middle of the air, so that it does not become a mako state.

本発明の混合装置を用いれば炭酸カルシウム、硫酸バンド、硫酸鉄、高分子凝集剤、活性炭等の難溶解物質を粉末あるいは粒体で搬送させ、搬入先で本発明の混合装置を用いて水溶液にすることにより、出荷元で溶液状態にしたものを運搬していたローリー車等のコストを下げる事が出来る。  If the mixing device of the present invention is used, a hardly soluble substance such as calcium carbonate, sulfuric acid band, iron sulfate, polymer flocculant, activated carbon or the like is transported as a powder or granules, and is brought into an aqueous solution using the mixing device of the present invention at the destination. By doing so, it is possible to reduce the cost of a lorry vehicle or the like that was transporting a solution in the shipping source.

次の本発明の他の形態として、本発明の混合装置を用いて汚濁水を処理する方法を説明する。
予め凝集剤を溶解した凝集剤の水溶液をパイプ等から供給ホッパー1に供給する。一方これと同時に懸濁粒子水をパイプ等により供給ホッパー1に供給する。またこれらと同時に接続管16から加圧水を供給すると、供給ホッパー1から導入された凝集剤水溶液と汚濁水は排出口2で混合され、接続管16から供給加圧水は溝10を通り外部に高圧ジェット水となって落下し、ハウジング14の出口部において一瞬にして、高圧ジェット水と混合されて排出される。このように本発明の混合装置のハウジング14の出口部から排出された水溶液は排出前の水溶液に比べて酸化還元電位が低くなる特長を有する。
更に、他の態様として、噴霧状のフラッシュ水をノズル等から供給ホッパー1に供給することによって、供給ホッパー1から導入されたフラッシュ水と凝集剤水溶液と懸濁粒子水は混合され、ハウジング14の出口部から、加圧水と混合されて排出される。このように本発明の混合装置のハウジング14の出口部から排出された水溶液は排出前の水溶液に比べて酸化還元電位が低く、凝集効果の高い中和反応を促進する特長を有する。
加圧水及びフラッシュ水に使用される水としては、水道水、工業用水、酸化還元電位を低くした水、排水を処理した水、濾過水等が挙げられる。
供給ホッパー1に供給する懸濁粒子水としては、沈殿池で沈殿したスラリー、スラリーを濃縮槽で濃縮した濃縮スラリー排水、スラリーを乾燥したものやベントナイト・カオリン・酸化チタン・ドラバイト等の粒子状物質を水に溶かした水溶液等が挙げられる。
As another embodiment of the present invention, a method for treating polluted water using the mixing apparatus of the present invention will be described.
An aqueous solution of the flocculant in which the flocculant is dissolved in advance is supplied to the supply hopper 1 from a pipe or the like. At the same time, suspended particulate water is supplied to the supply hopper 1 through a pipe or the like. At the same time, when pressurized water is supplied from the connecting pipe 16, the coagulant aqueous solution and the polluted water introduced from the supply hopper 1 are mixed at the discharge port 2, and the supplied pressurized water from the connecting pipe 16 passes through the groove 10 and is discharged to the outside via high-pressure jet water. And then, at the outlet of the housing 14, it is mixed with high-pressure jet water and discharged in an instant. Thus, the aqueous solution discharged from the outlet portion of the housing 14 of the mixing apparatus of the present invention has a feature that the oxidation-reduction potential is lower than that of the aqueous solution before being discharged.
Furthermore, as another aspect, by supplying spray-like flash water from the nozzle or the like to the supply hopper 1, the flash water introduced from the supply hopper 1, the flocculant aqueous solution, and the suspended particle water are mixed, and the housing 14 From the outlet, it is mixed with pressurized water and discharged. As described above, the aqueous solution discharged from the outlet portion of the housing 14 of the mixing apparatus of the present invention has a feature that the oxidation-reduction potential is lower than that of the aqueous solution before discharge, and promotes a neutralization reaction having a high aggregating effect.
Examples of the water used for the pressurized water and the flush water include tap water, industrial water, water having a low oxidation-reduction potential, water that has processed wastewater, and filtered water.
The suspended particulate water to be supplied to the supply hopper 1 includes slurry precipitated in a sedimentation basin, concentrated slurry drainage obtained by concentrating the slurry in a concentration tank, dried slurry, and particulate matter such as bentonite, kaolin, titanium oxide, and drabite. An aqueous solution in which is dissolved in water.

供給ホッパー1にフラッシュ水をノズル等から供給することによって、供給ホッパー1を洗浄することが出来る。  By supplying flush water to the supply hopper 1 from a nozzle or the like, the supply hopper 1 can be washed.

本発明の混合装置から排出された処理水は、懸濁粒子水中の汚濁粒子が凝集剤の作用によってフロック化されている。このように調製された処理水は、例えば、横流式沈殿池のフロック形成部に導入することによって、汚濁水の処理効率を高めることができる。
本発明の混合装置から排出された処理水は、フロック形成部に流入する前の汚濁水に比べて酸化還元電位が低く、フロック形成部において凝集効果の高い中和反応を促進する特長を有する。
In the treated water discharged from the mixing apparatus of the present invention, the contaminated particles in the suspended particle water are flocked by the action of the flocculant. The treated water prepared in this way can be improved in the efficiency of treating the contaminated water, for example, by introducing it into the floc forming part of the cross-flow type sedimentation basin.
The treated water discharged from the mixing apparatus of the present invention has a feature that the oxidation-reduction potential is lower than that of the polluted water before flowing into the floc forming part, and promotes a neutralization reaction having a high aggregating effect in the floc forming part.

また他の態様としてノズル等からフラッシュ水を横流式沈殿池のフロック形成部に供給し、またこれと同時に予め凝集剤を溶解した凝集剤の水溶液を各パイプ等により横流式沈殿池のフロック形成部に供給することによって汚濁水の処理効率を高めることができる。Further, as another embodiment, flush water is supplied from a nozzle or the like to the floc forming part of the cross-flow type sedimentation basin, and at the same time, an aqueous solution of the flocculant in which the flocculant is dissolved in advance is added to each floc forming part of the cross-flow type sedimentation basin By supplying to, the treatment efficiency of polluted water can be increased.

次の本発明の他の形態として、本発明の混合装置を用いて凝集沈殿処理水を処理し、急速濾過の損失水頭が低く、濾材の洗浄頻度を下げることができる方法を説明する。
供給ホッパー1に凝集剤水溶液を供給する。これと同時に接続管16から加圧水を供給すると、供給ホッパー1から導入された凝集剤水溶液はハウジング14の出口部において一瞬にして、加圧水と混合されて排出される。このように本発明の混合装置のハウジング14の出口部から排出された水溶液は排出前の水溶液に比べて酸化還元電位が低くなる特長を有する。凝集沈殿処理水に凝集剤を混合させ、急速濾過する際に、酸化還元電位が低い凝集剤水溶液を使用することで、凝集沈殿処理水に含まれる微量の残留物(フロックや微粒子、バクテリア、細菌等)の酸化還元電位を下げることによって短時間でフロック化させ、除去され易いようにして急速濾過することで損失水頭が低く、濾材の洗浄頻度を下げることができる
本発明方法によれば、接続管16から加圧水を供給すると供給ホッパー1から導入された液体・粉体を細かい粒子にして、混ざり合う時間を短くし、反応時間を短くすることが出来る。
As another embodiment of the present invention, a method will be described in which the coagulation sedimentation treated water is treated using the mixing apparatus of the present invention, the loss head of rapid filtration is low, and the washing frequency of the filter medium can be lowered.
An aqueous flocculant solution is supplied to the supply hopper 1. At the same time, when pressurized water is supplied from the connecting pipe 16, the flocculant aqueous solution introduced from the supply hopper 1 is instantaneously mixed with the pressurized water and discharged at the outlet of the housing 14. Thus, the aqueous solution discharged from the outlet portion of the housing 14 of the mixing apparatus of the present invention has a feature that the oxidation-reduction potential is lower than that of the aqueous solution before being discharged. When the flocculant is mixed with the coagulation sedimentation treatment water and rapid filtration is performed, by using an aqueous flocculant solution with a low oxidation-reduction potential, a small amount of residue (floc, fine particles, bacteria, bacteria) contained in the coagulation sedimentation treatment water Etc.) can be flocified in a short time by reducing the oxidation-reduction potential, and can be easily removed and rapidly filtered to reduce the head loss and reduce the frequency of washing of the filter medium. When pressurized water is supplied from the pipe 16, the liquid / powder introduced from the supply hopper 1 is made into fine particles, the mixing time can be shortened, and the reaction time can be shortened.

本発明方法によれば、従来アルミ系凝集剤を用いた場合イオン化したアルミニウムが処理されずに沈殿池から排出されることを防止することができる。
本発明方法によれば、処理する汚濁水は、例えば水道水の原水(ダム水、河川水、湖沼水)工業用水の原水、製造水の原水、下水排水、工場排水、製造排水等の汚濁水を好適に処理することができる。
According to the method of the present invention, it is possible to prevent ionized aluminum from being discharged from the sedimentation basin without being treated when a conventional aluminum flocculant is used.
According to the method of the present invention, the contaminated water to be treated is, for example, raw water for tap water (dam water, river water, lake water), industrial water, raw water for manufacturing water, sewage waste water, factory waste water, manufacturing waste water, etc. Can be suitably processed.

本発明の混合装置の断面図。Sectional drawing of the mixing apparatus of this invention. 本発明の混合装置の震動弁の1例を示す側面図。The side view which shows an example of the vibration valve of the mixing apparatus of this invention. 本発明の混合装置の本体の側面図。The side view of the main body of the mixing apparatus of this invention. 本発明の混合装置のハウジングの断面図。Sectional drawing of the housing of the mixing apparatus of this invention. 本発明の混合装置の震動弁の1実施態様を示す断面図。Sectional drawing which shows one embodiment of the vibration valve of the mixing apparatus of this invention.

符号の説明Explanation of symbols

1‥‥供給ホッパー
2‥‥排出口
3‥‥排出管
4‥‥震動弁
5‥‥弁本体
6‥‥棒状体
7‥‥本体
10‥‥溝
12‥‥内部室
13‥‥環状空間
14‥‥ハウジング
DESCRIPTION OF SYMBOLS 1 ... Supply hopper 2 ... Discharge port 3 ... Discharge pipe 4 ... Vibration valve 5 ... Valve body 6 ... Rod body 7 ... Body 10 ... Groove 12 ... Inner chamber 13 ... Annular space 14 ... ‥housing

Claims (2)

供給ホッパーと、内部軸方向に中央通路を有する本体と、前記本体を収納する内部室を有するハウジングからなり、混合物質と混合するための液体を前記ハウジングの側壁を通して前記内部室と前記本体との間に環状空間が形成されるように設けて、前記中央通路部を通過して落下する混合物質と流体とを合流混合させる混合装置において、前記供給ホッパーの排出管を前記本体の中央通路に挿入し、その供給ホッパーの排出口に、上部に棒状体を垂直に設けた震動弁を設け、ハウジングの内部室の壁面に湾曲した凹み部を設け、前記本体の外壁面に垂直状あるいは斜線状の溝を設けたことを特徴とする混合装置。 A supply hopper, a main body having a central passage in the inner axial direction, and a housing having an inner chamber for accommodating the main body, and a liquid for mixing with a mixed substance through the side wall of the housing between the inner chamber and the main body. In a mixing device that is provided so that an annular space is formed between them, and mixes and mixes the mixed substance and fluid that fall through the central passage portion, the discharge pipe of the supply hopper is inserted into the central passage of the main body In addition, the discharge valve of the supply hopper is provided with a vibration valve with a bar-like body provided vertically at the top, a curved recess is provided on the wall surface of the inner chamber of the housing, and the outer wall surface of the main body has a vertical or oblique shape. A mixing apparatus characterized by providing a groove. 請求項1の混合装置において、本体の中央通路に挿入する供給ホッパーの排出口の先端部が、前記本体の中央通路の先端部との面と同一になるかあるいは中央通路の先端部面より突出するように設けた請求項1記載の混合装置。
2. The mixing apparatus according to claim 1, wherein a front end portion of the discharge port of the supply hopper inserted into the central passage of the main body is the same as a surface of the main passage with the front end portion of the central passage or protrudes from a front end surface of the central passage. The mixing device according to claim 1, wherein the mixing device is provided.
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Cited By (2)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
CN107638719A (en) * 2017-11-07 2018-01-30 东莞市天合机电开发有限公司 A kind of scattered detention tank of precipitating reagent rotation
CN107651738A (en) * 2017-11-07 2018-02-02 东莞市天合机电开发有限公司 A kind of swing rod disperses the detention tank of precipitating reagent

Families Citing this family (1)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
CN114272806B (en) * 2022-01-04 2022-09-06 上海银鲨机器(集团)有限公司 Double-shaft paddle mixer with directional screening function

Family Cites Families (15)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JPS4830847Y1 (en) * 1968-01-25 1973-09-20
NL7306902A (en) * 1972-05-26 1973-11-28
JPS52108247A (en) * 1976-03-05 1977-09-10 Toshiko Teratani Hair curler
JPS56106833A (en) * 1980-12-25 1981-08-25 Ig Tech Res Inc Manufacture of polyisocyanurate foam having incombustibility
FR2510762A1 (en) * 1981-07-31 1983-02-04 Inst Francais Du Petrole SYSTEM FOR INTERCONNECTING THE ELEMENTS OF A RECEIVING DEVICE OF LARGE LENGTH, FOR DOUBLING THE NUMBER OF RECORDING TRACES CORRESPONDING TO THE RECEIVED SIGNALS
JPH01262990A (en) * 1988-04-12 1989-10-19 Mitani Sekisan Co Ltd Apparatus and method for treating muddy water
JPH0786032B2 (en) * 1988-05-23 1995-09-20 新田ゼラチン株式会社 Storage device
JPH0622666B2 (en) * 1989-09-28 1994-03-30 中部電力株式会社 Suspension preparation device
JPH05234A (en) * 1991-06-24 1993-01-08 Catalysts & Chem Ind Co Ltd Apparatus for mixing powder into liquid
JPH0885587A (en) * 1994-09-14 1996-04-02 Ebara Corp Hopper
JP3127119B2 (en) * 1996-03-26 2001-01-22 リョービ株式会社 Powder supply device
JPH1135093A (en) * 1997-07-15 1999-02-09 Kawasaki Refract Co Ltd Method and apparatus for preventing bridging of cone valve can
JP2002308445A (en) * 2001-04-18 2002-10-23 Komaki Kogyo Kk Quantitative powder and granular material supply device
JP3918657B2 (en) * 2002-06-28 2007-05-23 Jfeエンジニアリング株式会社 Method and apparatus for purifying contaminated soil
JP4169614B2 (en) * 2003-03-14 2008-10-22 東京電力株式会社 Wastewater treatment method

Cited By (2)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
CN107638719A (en) * 2017-11-07 2018-01-30 东莞市天合机电开发有限公司 A kind of scattered detention tank of precipitating reagent rotation
CN107651738A (en) * 2017-11-07 2018-02-02 东莞市天合机电开发有限公司 A kind of swing rod disperses the detention tank of precipitating reagent

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