JP3965491B2 - Alkaline ion water generator and acidic ion water generator - Google Patents

Alkaline ion water generator and acidic ion water generator Download PDF

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JP3965491B2
JP3965491B2 JP2003421699A JP2003421699A JP3965491B2 JP 3965491 B2 JP3965491 B2 JP 3965491B2 JP 2003421699 A JP2003421699 A JP 2003421699A JP 2003421699 A JP2003421699 A JP 2003421699A JP 3965491 B2 JP3965491 B2 JP 3965491B2
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林 重 太 郎 小
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本発明は、電解槽の陽極、陰極間に隔膜を介し電圧を印加して、水の電気分解によるアルカリイオン水生成装置並びに酸性イオン水生成装置に関する。   The present invention relates to an alkaline ionized water generator and an acidic ionized water generator by electrolysis of water by applying a voltage between an anode and a cathode of an electrolytic cell via a diaphragm.

pH2前後の強酸性或いはpH12前後の強アルカリ性を、長期間にわたり安定したpH値を保つイオン水を生成する製造装置と製造方法として、特許文献1が開示されている。   Patent Document 1 discloses a manufacturing apparatus and a manufacturing method for producing ionic water that maintains a strong pH of around pH 2 or strong alkalinity of around pH 12 and maintaining a stable pH value over a long period of time.

特許文献1の製造装置は、モンモリロナイトなどの結晶性粘土鉱物を主成分とするセラミックのイオン交換隔膜を用いて、その成分を溶解させることにより安定したpH値を保つイオン水を生成している。また、特殊素材のセラミックイオン交換隔膜を円筒形の密閉壺に形成して、同一の電解槽内に複数個配設し、処理水を密閉壺内に導き、電気分解を連続して行うことにより、pH値を高めていた。   The manufacturing apparatus of Patent Document 1 uses a ceramic ion-exchange membrane whose main component is a crystalline clay mineral such as montmorillonite, and generates ionic water that maintains a stable pH value by dissolving the components. In addition, by forming a ceramic ion exchange diaphragm made of special material into a cylindrical sealed tub and arranging a plurality of them in the same electrolytic cell, guiding the treated water into the sealed tub and performing electrolysis continuously The pH value was increased.

特許文献2には、処理容量が限られた特許文献1の欠点、及び汚染水の浄化などによる反応物(沈殿物)が回収可能な構造の電気分解を用いる水改質ユニットが開示されている。この発明では、平板状のモンモリロナイトなどの結晶性粘土鉱物を主成分とするセラミックのイオン交換隔膜を用いたユニットが提案されている。   Patent Document 2 discloses a water reforming unit using electrolysis having a structure capable of recovering a reaction product (precipitate) by purifying contaminated water and the disadvantages of Patent Document 1 having a limited processing capacity. . In the present invention, a unit using a ceramic ion exchange diaphragm mainly composed of a crystalline clay mineral such as flat montmorillonite has been proposed.

これらの、長期安定した強いアルカリ性或いは酸性のpH値の処理水を得るイオン水生成装置は、特殊なセラミック隔膜の制約から小型の壺状電解室或いは20〜30cm角の小型板状隔膜で仕切られた電解室を電解槽中に並べて電気分解を連続して行う方法がとられていた。   These ionic water generators that obtain treated water with a strong alkaline or acidic pH value that is stable for a long period of time are partitioned by a small bowl-shaped electrolysis chamber or a small plate-shaped diaphragm of 20 to 30 cm square due to the limitations of a special ceramic diaphragm. A method has been adopted in which electrolysis is continuously performed by arranging the electrolysis chambers in an electrolytic cell.

このため、廃水処理、水質維持処理などを単位時間当たり大量に行う場合は、限られた前記小型方形の隔膜による電解槽空間で、密閉状態で行う従来のイオン水生成装置では、利用ができない問題があった。   For this reason, when wastewater treatment, water quality maintenance treatment, etc. are performed in large quantities per unit time, conventional ion water generators that are sealed in the electrolytic cell space with the limited small square diaphragm cannot be used. was there.

特開平8−24865号公報(第2,3,4頁、第1図)JP-A-8-24865 (pages 2, 3, 4 and FIG. 1) 特願2002−380357号公報(第2,3,4頁、第1図)Japanese Patent Application No. 2002-380357 (pages 2, 3, 4 and 1)

本発明は、前記の問題に鑑みてなされたもので、処理水の電気分解によるアルカリイオン化或いは酸性イオン化処理を円筒状隔膜の密閉管路内で一方向へ連続的に単位時間当たり大量に処理水を通過させて強イオン水を生成処理可能な生成装置を提供することを課題とする。   The present invention has been made in view of the above-mentioned problems, and performs alkaline ionization or acidic ionization treatment by electrolysis of treated water in a large amount per unit time continuously in one direction within a sealed duct of a cylindrical diaphragm. It is an object of the present invention to provide a generation device that can pass strong water to generate strong ion water.

また、電気分解ユニットを複数直列或いは並列に接続して、河川水或は坑道廃水などの大量の流水をイオン化する生成装置を提供することを課題とする。   It is another object of the present invention to provide a generating apparatus that ionizes a large amount of flowing water such as river water or mine drainage water by connecting a plurality of electrolysis units in series or in parallel.

本発明のアルカリイオン水生成装置は、棒状又はパイプ状の負の中心電極の中心軸に円筒型に成形されたイオン交換隔膜の中心軸を合わせて所定の間隙距離を維持して配設し、
その円筒状隔膜の外側に円筒型に成形されたメッシュ状又は電解溶液透過性の正の外側筒電極の中心軸を合わせて所定の間隙距離を維持して配設し、
前記円筒状隔膜の外側では電解質溶液を循環させ、その隔壁の内側では下部より処理水を流入させて、前記正・負電極間に直流電圧を印加して、電気分解を行わせ、隔壁上部より処理水をアルカリイオン化して流出させるアルカリイオン水生成装置であって、
前記隔膜は、最大長が0.5〜2mm径の範囲に入る粒状或いは破砕された結晶性粘土鉱物を主体としたセラミックに対し、85〜95℃に加熱した水溶性高分子材を10〜30重量%混入して混練し、補強用布状繊維上に圧出成形して平板成形材とし、直後に円筒状の型材に捲き付けて乾燥させた、円筒状のセラミック混入樹脂バインダー層からなる隔膜構造を備え、
その隔膜の下部には、そのフランジから上下方向にそれぞれ所定長のパイプを有し、そのパイプの外径は、前記隔膜の内径に合わせ、上側パイプは隔膜下端円周内側に接続可能とし、下側パイプは前記処理水の流入パイプの内側に接続可能とする下部接続部材を備え、
前記隔膜の上部には、外径が前記隔膜内径に合わせたパイプを有し、そのパイプ下側と隔膜上端円周内側に接続可能とし、そのパイプ上側端部は前記負の中心電極端子接続用フランジを有し、さらに処理水のアルカリイオン水流出口パイプ接続部とを有する上部接続部材を備え、
前記隔膜円筒部外側には、前記正の外円筒電極が前記所定の間隙距離を維持するための隔膜の外側の上下端2ヶ所に嵌められた電気絶縁性のリングスペーサを備え、
前記隔膜の外側まで前記正の外円筒電極を透過して電解質溶液を循環させる為の電解質溶液を収容する電解槽を備え、
前記上部接続部材のパイプ中間部には、その上部接続部材と、その上側でフランジにより連結する負の中心電極端子板および負の中心電極端子と、上部接続部材の下側にフランジとスペーサにより連結する隔膜及び正の外円筒電極と、前記隔膜の下端部に下部接続部材を介して連結する処理水流入パイプと、それを連結する処理水入口パイプ接続部とを接続した電気分解ユニットをそのまま保持する状態で溶着されたユニット保持板材を備え、
前記電解槽の上部には、前記保持部材に保持された、前記電気分解ユニットを装着したまま、その電解槽の上側から挿入して電気分解ユニットを電解質溶液に沈めて、前記保持板材の周縁を電解槽の上側に載せてネジ留できる保持板材受口部と、前記電解質溶液から発生する外円筒極側ガス抜き孔部とを備えることを特徴とする。
The alkaline ionized water generating device of the present invention is arranged by maintaining a predetermined gap distance by aligning the central axis of the ion-exchange membrane formed into a cylindrical shape with the central axis of the negative central electrode in the shape of a rod or pipe.
Maintaining a predetermined gap distance by aligning the central axis of the mesh-shaped or electrolytic solution-permeable positive outer cylinder electrode formed in a cylindrical shape outside the cylindrical diaphragm,
The electrolyte solution is circulated outside the cylindrical diaphragm, the treated water is allowed to flow from the bottom inside the partition, and a DC voltage is applied between the positive and negative electrodes to perform electrolysis, from above the partition. An alkaline ionized water generating apparatus for alkalinely ionizing treated water to flow out,
The diaphragm is made of 10-30 water-soluble polymer material heated to 85-95 ° C with respect to a ceramic mainly composed of granular or crushed crystalline clay mineral having a maximum length of 0.5-2 mm. A diaphragm composed of a cylindrical ceramic-mixed resin binder layer mixed and kneaded by weight, extruded onto a reinforcing fabric fiber to form a flat plate molding material, and immediately spread on a cylindrical mold material and dried. With structure,
The lower part of the diaphragm has pipes each having a predetermined length in the vertical direction from the flange. The outer diameter of the pipe matches the inner diameter of the diaphragm, and the upper pipe can be connected to the inner circumference of the lower end of the diaphragm. The side pipe includes a lower connection member that can be connected to the inside of the treated water inflow pipe,
The upper part of the diaphragm has a pipe whose outer diameter matches the inner diameter of the diaphragm, and can be connected to the lower side of the pipe and the inner circumference of the upper end of the diaphragm, and the upper end of the pipe is used for connecting the negative central electrode terminal. An upper connection member having a flange and further having an alkali ion water outlet pipe connection part of the treated water;
Outside the diaphragm cylindrical portion, the positive outer cylindrical electrode is provided with electrically insulating ring spacers fitted at two upper and lower ends on the outer side of the diaphragm for maintaining the predetermined gap distance,
An electrolytic cell containing an electrolyte solution for circulating the electrolyte solution through the positive outer cylindrical electrode to the outside of the diaphragm;
Connected to the pipe intermediate part of the upper connecting member by the upper connecting member, the negative central electrode terminal plate and the negative central electrode terminal connected by the flange on the upper side, and the flange and spacer on the lower side of the upper connecting member The electrolysis unit that holds the diaphragm and the positive outer cylindrical electrode, the treated water inflow pipe connected to the lower end of the diaphragm via the lower connecting member, and the treated water inlet pipe connecting part for holding it is held as it is. Unit holding plate material welded in a state to
With the electrolysis unit held by the holding member attached to the upper part of the electrolytic cell, the electrolysis unit is inserted from the upper side of the electrolytic cell and the electrolysis unit is submerged in the electrolyte solution, so that the periphery of the holding plate is It is characterized by comprising a holding plate material receiving part that can be screwed on the upper side of the electrolytic cell, and an outer cylindrical pole side gas vent hole part generated from the electrolyte solution.

また、前記処理水流入パイプには、堆積物をエアリフトさせる圧縮空気入力用パイプ端子を備えることを特徴とする。   Further, the treated water inflow pipe includes a compressed air input pipe terminal for air-lifting the deposit.

また、前記電解層の横方向に沿って一端側から順次前記処理水パイプ接続部、処理水流水パイプ及び正電極(端子)、負電極(端子)及び隔膜、アルカリイオン水流出口パイプ接続部が一列に配列される構造の単位電気分解ユニットを備えて、
その電解槽の奥行方向に沿って、前記単位電気分解ユニットをn段配設できるように、前記電解槽の上部にnヶ所の前記保持板材受口部を備え、
各単位電気分解ユニットの前記処理水入り口部に接続し、n段分の処理水を流入させる総処理水入口パイプ部と、
各単位電気分解ユニットの前記アルカリイオン水流出口部に接続し、n段分のアルカリイオン水を流出させる総アルカリイオン水出口パイプ部とを備え、
n段の単位電気分解ユニットを並列に動作させることを特徴とする。
Further, the treated water pipe connecting portion, the treated water flowing water pipe and the positive electrode (terminal), the negative electrode (terminal) and the diaphragm, and the alkali ion water outlet pipe connecting portion are sequentially arranged from one end side along the lateral direction of the electrolytic layer. Comprising a unit electrolysis unit of a structure arranged in
Along with the depth direction of the electrolytic cell, the unit electrolysis unit is provided with n holding plate material receiving portions at the upper part of the electrolytic cell so that the unit electrolysis unit can be arranged in n stages,
Connected to the treated water inlet part of each unit electrolysis unit, a total treated water inlet pipe part into which treated water for n stages flows,
It is connected to the alkaline ion water outlet part of each unit electrolysis unit, and comprises a total alkaline ion water outlet pipe part for allowing n stages of alkaline ion water to flow out,
An n-stage unit electrolysis unit is operated in parallel.

また、前記電解槽の第n段目の単位電気分解ユニットに近い位置から電解質溶液をポンプで汲み上げ、第1段目の単位電気分解ユニットに近い位置へ、その電解質溶液を循環させる循環パイプを備えることを特徴とする。   In addition, a circulation pipe is provided for pumping up the electrolyte solution from a position near the n-th unit electrolysis unit of the electrolytic cell and circulating the electrolyte solution to a position near the first stage unit electrolysis unit. It is characterized by that.

また、前記電解槽の横方向に沿って、一端側から順次前記アルカリイオン水流出口部、イオン水流出パイプ、負の中心電極(端子)及び正電極(端子)、処理水入口部が一列に配列される構造の第1の単位電気分解ユニットと、さらに、前記単位電気分解ユニットに順次接続する前記処理水入口部、正電極(端子)、負電極(端子)及び隔膜、アルカリイオン水出口部、イオン水流出パイプ部が一列に配列される反転構造の第2の単位電気分解ユニットを備え、
その電解槽の奥行方向に沿って直列に接続した前記第1及び第2の単位電気分解ユニットをn段配設できるように前記電解槽の上部には横方向に2ヶ所の前記保持板材受口部を奥行き方向にn段、合計n×2ヶ所備え、
第1の単位電気分解ユニットの前記アルカリイオン水流出部に接続し、n段分の処理水を流入させる横方向一端側に配設する第1のイオン水パイプ入口部と、
第2の単位電気分解ユニットの前記アルカリイオン水流出部に接続し、n段分の処理水を流入させる横方向他端側に配設する第2のイオン水パイプ入口部と、
第1及び第2の単位電気分解ユニットの前記処理水流出口部に接続し、n段×2個のアルカリイオン水を流出させる総処理水出口パイプ部とを備え、
n段×2個の単位電気分解ユニットを、2個直列n段並列に動作させることを特徴とする。
In addition, the alkaline ion water outlet, the ion water outlet pipe, the negative center electrode (terminal) and the positive electrode (terminal), and the treated water inlet are arranged in a row from one end side along the horizontal direction of the electrolytic cell. A first unit electrolysis unit having a structure, and further, the treated water inlet, the positive electrode (terminal), the negative electrode (terminal) and the diaphragm, which are sequentially connected to the unit electrolysis unit, the alkaline ion water outlet, A second unit electrolysis unit having an inverted structure in which ion water outflow pipe portions are arranged in a line;
Two holding plate material receiving ports in the lateral direction are provided above the electrolytic cell so that n stages of the first and second unit electrolysis units connected in series along the depth direction of the electrolytic cell can be arranged. There are n stages in the depth direction, a total of nx 2 locations,
A first ionic water pipe inlet connected to the alkaline ionized water outflow part of the first unit electrolysis unit and disposed on one side in the lateral direction to allow treatment water for n stages to flow;
A second ionic water pipe inlet connected to the alkaline ion water outflow part of the second unit electrolysis unit and disposed on the other side in the lateral direction through which treated water for n stages flows.
Connected to the treated water outlet of the first and second unit electrolysis units, and comprises a total treated water outlet pipe for allowing n stages × 2 pieces of alkaline ionized water to flow out,
Two unit electrolysis units of n stages × 2 units are operated in series and n stages in parallel.

また、棒状又はパイプ状の負の中心電極の中心軸に円筒型に成形されたイオン交換隔膜の中心軸を合わせて所定の間隙距離を維持して配設し、
その円筒状隔膜の外側に円筒型に成形されたメッシュ状又は電解溶液透過性の正の外円筒電極の中心軸を合わせて所定の間隙距離を維持して配設し、
前記円筒状隔膜の外側には電解質溶液を循環させ、その隔壁の内側には処理水を流入させて、前記正・負電極間に電圧を印加して、電気分解を行わせ、処理水をアルカリイオン化して流出させるアルカリイオン水生成装置であって、
前記隔膜は、0.5〜2mm径の粒状或いは破砕された結晶性粘土鉱物を主体としたセラミックに対し、85〜95℃に加熱した水溶性高分子材を10〜30重量%に混入して混練し、補強用布状繊維上に圧出成形して平板成形材とし、直後に円筒状の型材に捲き付けて乾燥させた、円筒状のセラミック混入樹脂バインダー層からなる隔膜構造を備え、
その隔膜の下部には、そのフランジから上下方向にそれぞれ所定長のパイプを有し、そのパイプの外径は、前記隔膜の内径に合わせ、上側パイプは隔膜下端円周内側に接続可能とし、下側パイプは前記処理水流入パイプの内側に接続可能とする下部接続部材を備え、
前記隔膜の上部には、外径が前記隔膜内径に合わせたパイプを有し、そのパイプ下側と隔膜上端円周内側に接続可能とし、そのパイプ上側端部は前記負電極端子接続用フランジを有し、さらに処理水のアルカリイオン水流出口を有する上部接続部材を備え、
前記隔膜円筒部外側には、前記正電極が前記所定の間隙距離を維持するための隔膜の外側の上下端2ヶ所に嵌められた電気絶縁性のリングスペーサを備え、
前記上部接続部材と、その上側でフランジにより連結する負電極端子板及び負電極と、上部接続部材の下側に連結する隔膜及び正電極と、前記隔膜の下端部に下部接続部材を介して連結する処理水流入パイプと、それに連結する処理水入力部とを接続した高密度用電気分解ユニットを備え、
その電気分解ユニットを横方向にm列、奥行き方向にn列、m×n個の行列に電解に配設し、
各電気分解ユニットの上部のアルカリイオン水流出口m×n個を総合する総合アルカリイオン水流出口パイプと、
各電気分解ユニットの下部の処理水入口m×n個を総合する総合処理水流入口パイプと、
各電気分解ユニットの負電極m×n個を接続した負電極端子と、
各電気分解ユニットの正電極m×n個を接続した正電極端子とを備えることを特徴とする。
In addition, the central axis of the cylindrical ion-exchange membrane is aligned with the central axis of the rod-shaped or pipe-shaped negative central electrode to maintain a predetermined gap distance,
A mesh-shaped or electrolytic solution-permeable positive outer cylindrical electrode formed in a cylindrical shape outside the cylindrical diaphragm is aligned with the central axis of the positive diaphragm electrode to maintain a predetermined gap distance,
An electrolyte solution is circulated outside the cylindrical diaphragm, and treated water is allowed to flow inside the partition wall. A voltage is applied between the positive and negative electrodes to cause electrolysis, and the treated water is alkalinized. An alkaline ionized water generator that ionizes and flows out,
The diaphragm is made by mixing 10 to 30% by weight of a water-soluble polymer material heated to 85 to 95 ° C. with respect to a ceramic mainly composed of 0.5 to 2 mm diameter granular or crushed crystalline clay mineral. Kneaded, extruded on a reinforcing cloth-like fiber to form a flat plate molding material, and immediately after being spread on a cylindrical mold material and dried, comprising a diaphragm structure composed of a cylindrical ceramic-mixed resin binder layer,
The lower part of the diaphragm has pipes each having a predetermined length in the vertical direction from the flange. The outer diameter of the pipe matches the inner diameter of the diaphragm, and the upper pipe can be connected to the inner circumference of the lower end of the diaphragm. The side pipe includes a lower connection member that can be connected to the inside of the treated water inflow pipe,
The upper part of the diaphragm has a pipe whose outer diameter matches the inner diameter of the diaphragm, and can be connected to the lower side of the pipe and the inner circumference of the upper end of the diaphragm, and the upper end of the pipe has the flange for connecting the negative electrode terminal. Further comprising an upper connecting member having an alkaline ion water outlet for the treated water,
Outside the diaphragm cylindrical portion, the positive electrode is provided with electrically insulating ring spacers fitted at two upper and lower ends on the outer side of the diaphragm for maintaining the predetermined gap distance,
The upper connection member, a negative electrode terminal plate and a negative electrode connected by a flange on the upper side, a diaphragm and a positive electrode connected to the lower side of the upper connection member, and a lower connection part connected to a lower end portion of the diaphragm A high-density electrolysis unit that connects a treated water inflow pipe and a treated water input connected to the treated water inflow pipe,
The electrolysis unit is arranged for electrolysis in m columns in the horizontal direction, n columns in the depth direction, and m × n matrix,
A total alkali ion water outlet pipe that combines m × n alkali ion water outlets at the top of each electrolysis unit;
An integrated treated water inlet pipe that synthesizes m × n treated water inlets at the bottom of each electrolysis unit;
A negative electrode terminal connecting m × n negative electrodes of each electrolysis unit;
And a positive electrode terminal connected to m × n positive electrodes of each electrolysis unit.

本発明の酸性イオン水生成装置は、請求項1、3、5、6のいずれか1項に記載のアルカリイオン水生成装置において、正・負電極端子を逆電極に接続することにより、処理水を酸性イオン化して、アルカリ水流出口部に酸性イオン水を生成することを特徴とする。 The acidic ionic water generator of the present invention is the alkaline ionic water generator according to any one of claims 1, 3, 5, and 6, wherein the positive / negative electrode terminal is connected to the reverse electrode, whereby treated water Is acidic ionized to produce acidic ion water at the alkaline water outlet.

本発明のアルカリイオン水或いは酸性水生成装置は、処理水を円筒状隔膜管路内で連続して、安定的なPh値を維持するイオン化水とすることができる。また、複数の単位電気分解ユニットを並列・直列を自在に連結できる構造であるため、単位時間当たり大量の水のイオン化が可能であり、処理目的に合わせて、最適な規模の生成装置を安価に提供することができる。   The alkaline ionized water or acidic water generating apparatus of the present invention can make treated water into ionized water that maintains a stable Ph value continuously in a cylindrical diaphragm channel. In addition, since the unit electrolysis units can be connected in parallel or in series, a large amount of water can be ionized per unit time. Can be provided.

本発明のアルカリイオン水生成装置ならびに酸性イオン水生成装置の実地の形態を図面に基づいて詳細に説明する。   Embodiments of the alkaline ionized water generator and the acidic ionized water generator of the present invention will be described in detail with reference to the drawings.

図1は本発明のアルカリイオン水生成装置の第1の実施の形態を示し、(a)は使用している円筒状隔膜10(イオン交換隔膜)の円筒中心軸を通る断面図、(b)は平面図である。   FIG. 1 shows a first embodiment of an alkaline ionized water generator according to the present invention, in which (a) is a sectional view through a cylindrical central axis of a cylindrical diaphragm 10 (ion exchange diaphragm) used, (b). Is a plan view.

ここで、その円筒中心軸には棒状またはパイプ状の負の中心電極11が配設される。負の中心電極11は例えばステンレス製など腐食に強い金属を用いる。   Here, a rod-shaped or pipe-shaped negative center electrode 11 is disposed on the cylindrical central axis. The negative center electrode 11 is made of a metal resistant to corrosion, such as stainless steel.

負の中心電極11と円筒状隔膜10とは、その間で所定の間隙距離11dを維持できるようにその上端側は後述する中心電極端子11aにより中心電極11の下端部を固定している。   The lower end of the center electrode 11 is fixed to the upper end side of the negative center electrode 11 and the cylindrical diaphragm 10 by a center electrode terminal 11a described later so that a predetermined gap distance 11d can be maintained between them.

なお、その中心電極11の下端部も、後述する中心電極支持用羽根部材300a(図6(a)の図示参照)を使用し、さらに、正確に間隙距離11dを維持するようにしてもよい。   The lower end portion of the center electrode 11 may also use a center electrode supporting blade member 300a (see the illustration in FIG. 6A), which will be described later, and more accurately maintain the gap distance 11d.

その円筒状隔膜10の外側には、円筒状に成形され、電解溶液が自由に通過できるメッシュ状(例えば、カーボン繊維などで製作した円筒、或いは複数の小径口孔を明けた金属円筒、或いは金属網で製作した円筒)又は電解溶液透過性の正の外円筒電極12の中心軸を合わせて、円筒状隔膜10との所定の間隙距離12dを維持して配設する。   On the outside of the cylindrical diaphragm 10, it is formed into a cylindrical shape, and a mesh shape (for example, a cylinder made of carbon fiber or the like, a metal cylinder with a plurality of small-diameter holes, or metal The cylinder is made of a mesh) or the central axis of the electrolyte solution permeable positive outer cylindrical electrode 12 is aligned and maintained at a predetermined gap distance 12d with the cylindrical diaphragm 10.

16は電解槽を示し、その中に電解質溶液17がその溶液水位17aまで入っている。   Reference numeral 16 denotes an electrolytic cell in which an electrolyte solution 17 is contained up to the solution water level 17a.

ここでイオン水生成動作を説明する。すなわち、円筒状隔膜10の外側では電解質溶液17を循環させ、円筒状隔膜10の内側では、その下部(処理水隔膜入口10in)より処理水を流入させ、正、負電極端子12a、11a間に直流電圧を印加して電気分解を行わせ、円筒状隔膜10の上部(イオン水隔膜出口10out)より処理水をアルカリイオン化して流出させる。   Here, the ion water generating operation will be described. That is, the electrolyte solution 17 is circulated on the outside of the cylindrical diaphragm 10, and the treated water is introduced into the cylindrical diaphragm 10 from the lower part (treated water diaphragm inlet 10in) between the positive and negative electrode terminals 12a and 11a. Electrolysis is performed by applying a DC voltage, and the treated water is alkali ionized and discharged from the upper part of the cylindrical diaphragm 10 (ionic water diaphragm outlet 10out).

ここで用いる円筒状隔膜10について説明する。円筒状隔膜10は、予め珪酸4面体とアルミナ8面体とが結合した結晶性粘土鉱物を焼成したセラミックを最大長が0.5〜2mmの範囲に入る粒状に加工しておき、その粒状セラミックに対して85〜95℃に加熱した水溶性高分子材を10〜30重量%混合して混練し、補強用布状織物上に圧出成形して、平板成形材とし、さらに、その直後に円筒状の型枠に捲きつけて、85〜95℃以下の温度で成形乾燥させたセラミック混入樹脂バインド層の隔膜構造である。   The cylindrical diaphragm 10 used here is demonstrated. The cylindrical diaphragm 10 is obtained by processing a ceramic obtained by firing a crystalline clay mineral, in which a silicic acid tetrahedron and an alumina octahedron are previously bonded, into a granular shape having a maximum length in the range of 0.5 to 2 mm. On the other hand, 10 to 30% by weight of a water-soluble polymer heated to 85 to 95 ° C. is mixed and kneaded, and is extrusion-molded on a reinforcing cloth-like woven fabric to form a flat plate molding material. This is a diaphragm structure of a ceramic-mixed resin binding layer that is wound on a shaped mold and molded and dried at a temperature of 85 to 95 ° C. or lower.

前記水溶性高分子材は、少なくとも、ポリビニルアルコール、ポリアクリル酸ナトリウム、ポリエチレンオキサイドのいずれかの高分子材か、又は寒天、澱粉、カゼイン、ゼラチン、アラビアガムなどの天然高分子材である。   The water-soluble polymer material is at least a polymer material selected from polyvinyl alcohol, sodium polyacrylate, and polyethylene oxide, or a natural polymer material such as agar, starch, casein, gelatin, and gum arabic.

また、前記補強用布状織物は、ガラス繊維、炭素繊維、ポリプロピリン系繊維、ビニロン系繊維、アラミド系繊維のいずれかの素材からなる補強用布状織物である。   The reinforcing cloth-like fabric is a reinforcing cloth-like fabric made of any one of glass fiber, carbon fiber, polypropylin fiber, vinylon fiber, and aramid fiber.

尚、前記水溶性高分子材は、温度が85〜95℃では、前記補強用布状織物に浸透し、その織物の表側、裏側の表面及び内部に含浸して、その後乾燥されて隔膜を形成する。電解槽内の円筒状隔膜10は、水温では固体膨潤状態となる。   The water-soluble polymer material penetrates the reinforcing cloth-like woven fabric at a temperature of 85 to 95 ° C., impregnates the front and back surfaces and the inside of the woven fabric, and then is dried to form a diaphragm. To do. The cylindrical diaphragm 10 in the electrolytic cell is in a solid swelling state at the water temperature.

以上のように製作された円筒状隔膜10は、電解槽16の中で電極に直流電圧が印加されて動作している際に、その円筒状隔膜10中に混入されているセラミック粒子の前記結晶性粘土鉱物分子を電解質溶液17中に溶解させる。そこで、直流電圧印加により生成されるマイナスイオンまたはプラスイオンを安定状態に保つ。この現象により円筒状隔膜10の内側に流された処理水を安定したアルカリイオン水または酸性イオン水にすることができる。すなわち、従来の電気分解水のように、短時間(或いは数日)でpHが中性化することがない。   When the cylindrical diaphragm 10 manufactured as described above is operated by applying a DC voltage to the electrodes in the electrolytic cell 16, the crystal of ceramic particles mixed in the cylindrical diaphragm 10 is operated. The clay mineral molecules are dissolved in the electrolyte solution 17. Therefore, negative ions or positive ions generated by applying a DC voltage are kept in a stable state. By this phenomenon, the treated water that has flowed inside the cylindrical diaphragm 10 can be made into stable alkaline ionized water or acidic ionized water. That is, unlike conventional electrolyzed water, the pH does not become neutral in a short time (or several days).

その円筒状隔膜10の下部(図1(a)に示す処理水隔膜入口10in)には、フランジ13aから上下方向にそれぞれ所定長延びるパイプ13bを有して、そのパイプ13bの外径は円筒状隔膜10の内径に合わせて上側のパイプ13bの円筒状隔膜10下端円筒内側に挿入され接続可能・着脱可能とし、下側のパイプ13bは前記処理水の流入パイプ18の内側へ挿入され接続可能・着脱可能な下部接続部材13を備える。   The lower part of the cylindrical diaphragm 10 (the treated water diaphragm inlet 10in shown in FIG. 1 (a)) has pipes 13b each extending a predetermined length in the vertical direction from the flange 13a. The outer diameter of the pipe 13b is cylindrical. It is inserted into the cylindrical bottom end of the cylindrical diaphragm 10 of the upper pipe 13b according to the inner diameter of the diaphragm 10 and can be connected. The lower pipe 13b is inserted into the inflow pipe 18 of the treated water and can be connected. A detachable lower connecting member 13 is provided.

一方、その円筒状隔膜10の上部(図1(a)に示すイオン水隔膜出口10out)には、外径が円筒状隔膜10内径に合わせたパイプ14aを有し、そのパイプ14a下側を円筒状隔膜10上端円周内側に挿入され接続可能・着脱可能とし、そのパイプ14aの上側端部は、負の中心電極端子接続用フランジ14bを有し、さらに、そのパイプ14aの側面には処理水のアルカリイオン水流出口パイプ接続部14cを有する上部接続部材14を備える。   On the other hand, an upper part of the cylindrical diaphragm 10 (ionic water diaphragm outlet 10out shown in FIG. 1A) has a pipe 14a whose outer diameter matches the inner diameter of the cylindrical diaphragm 10, and the lower side of the pipe 14a is cylindrical. The upper end of the pipe 14a has a negative center electrode terminal connecting flange 14b inserted into the inner circumference of the upper periphery of the diaphragm 10 and has a treated water on the side surface of the pipe 14a. The upper connecting member 14 having the alkaline ion water outlet pipe connecting portion 14c is provided.

円筒状隔膜10の円筒部外側には、正の外円筒電極12が所定の間隙距離12dを維持するための隔膜の外側の上下端2ヶ所に嵌められた電気絶縁性のリングスペーサ15を備える。   On the outer side of the cylindrical portion of the cylindrical diaphragm 10, there are provided electrically insulating ring spacers 15 fitted at two upper and lower ends on the outer side of the diaphragm for the positive outer cylindrical electrode 12 to maintain a predetermined gap distance 12 d.

上部接続部材14のパイプ14aの中間位置にはユニット保持部材19が半田付けなどで溶着されている。ねじ等によりパッキングを介して固定する密着構造であってもよい。電解質溶液が密封されるような構造であればよい。   A unit holding member 19 is welded to the middle position of the pipe 14a of the upper connecting member 14 by soldering or the like. It may be a close contact structure that is fixed via a packing with screws or the like. Any structure that seals the electrolyte solution may be used.

そのユニット保持部材19には電気分解ユニット20が溶着されている。図2にもその電気分解ユニット20が図示されているが、単位電気分解ユニットとして接続されている部材群を以下に説明する。   An electrolysis unit 20 is welded to the unit holding member 19. Although the electrolysis unit 20 is also illustrated in FIG. 2, a group of members connected as a unit electrolysis unit will be described below.

その部材群は、上下接続部材14と、その上側でフランジ14bにより連結する負の中心電極端子板11b及び負の中心電極端子11aと、上部接続部材14の下側外周で連結する円筒状隔膜10及び前記リングスペーサ15を介して連結する正の外円筒電極12と、円筒状隔膜10の下端部に下部接続部材13を介して連結する処理水入口パイプ18と、それと連結する処理水入口パイプ接続部18aとを少なくとも接続した部材からなる。   The member group includes a vertical diaphragm member 14, a negative central electrode terminal plate 11 b and a negative central electrode terminal 11 a that are coupled by a flange 14 b on the upper side thereof, and a cylindrical diaphragm 10 that is coupled on the lower outer periphery of the upper connection member 14. And the positive outer cylindrical electrode 12 connected via the ring spacer 15, the treated water inlet pipe 18 connected to the lower end of the cylindrical diaphragm 10 via the lower connecting member 13, and the treated water inlet pipe connection connected thereto. It consists of the member which connected the part 18a at least.

以上の部材群からなる電気分解ユニット20がユニット保持部材19に溶着されている状態を図2に示す。図2では、保持部材19を電解槽16の上部にある保持板受口部16aの周辺にあるネジ受16cから固定ネジ19aを取外し上方へ引き上げた状態を示す。   FIG. 2 shows a state in which the electrolysis unit 20 composed of the above member group is welded to the unit holding member 19. FIG. 2 shows a state in which the holding member 19 is removed from the screw receiver 16c around the holding plate receiving portion 16a at the top of the electrolytic cell 16 and is pulled upward.

保持部材19を上方へ引き上げることにより電気分解ユニット20を電解質溶液17から引き上げ、部材の調整或いは取替え、再組立・修理を容易に行うことができる。   By pulling up the holding member 19, the electrolysis unit 20 can be lifted from the electrolyte solution 17, and the member can be easily adjusted or replaced, and reassembled and repaired easily.

なお、図1(b)の平面図には、電解槽16の上面にある保持板受口部16aが破線で示されている。   In the plan view of FIG. 1B, the holding plate receiving portion 16a on the upper surface of the electrolytic cell 16 is indicated by a broken line.

図1、図2において,12aは正の外円筒電極端子を示し、電解槽16の内部で電線により正の外円筒電極12と接続されている。   In FIGS. 1 and 2, reference numeral 12 a denotes a positive outer cylindrical electrode terminal, which is connected to the positive outer cylindrical electrode 12 by an electric wire inside the electrolytic cell 16.

処理水流水パイプ18は第1実施例ではJ字状で円筒状隔膜10の下部からユニット保持板材19を通り抜け、その保持部材19にハンダ付け或いは溶着されている。   The treated water flow pipe 18 is J-shaped in the first embodiment and passes through the unit holding plate material 19 from the lower part of the cylindrical diaphragm 10 and is soldered or welded to the holding member 19.

その処理水流水パイプ18の出口付近には圧縮空気入力用バルブ端子22(電解槽16の上部側面に設けてある)からのエアーを入れる空気入力口22aがある。時々、エアーを入れることにより処理水流水パイプ18の底面付近に蓄積された沈殿固体物を取り除くことができる。   Near the outlet of the treated water pipe 18 is an air input port 22a for receiving air from a compressed air input valve terminal 22 (provided on the upper side surface of the electrolytic cell 16). Occasionally, it is possible to remove the precipitated solid accumulated in the vicinity of the bottom surface of the treated water flow pipe 18 by introducing air.

21は、補強アングル材(PVC)を示し、電気分解ユニット20の重量を受けるユニット保持部材19による電解槽16の受口部16aの耐荷重を増加させる。   Reference numeral 21 denotes a reinforcing angle member (PVC), which increases the load resistance of the receiving portion 16 a of the electrolytic cell 16 by the unit holding member 19 that receives the weight of the electrolysis unit 20.

図1に示した第1の実施例のアルカリイオン水生成装置の動作は以下のようになる。電解質溶液17は電解槽16の中で循環させる(図1には図示していない)。また、正の外円筒電極端子12aと負の中心電極端子11a間に直流電圧を印加しておく。   The operation of the alkaline ionized water generator of the first embodiment shown in FIG. 1 is as follows. The electrolyte solution 17 is circulated in the electrolytic cell 16 (not shown in FIG. 1). A DC voltage is applied between the positive outer cylindrical electrode terminal 12a and the negative center electrode terminal 11a.

アルカリイオン水に処理したい水を、処理水入口パイプ接続部18aから流入させる。この流入水は処理水流水パイプ18を通り、円筒状隔膜10の下部10inに達する。ここで、その処理水は円筒状隔膜10と負の中心電極の間を上昇し、その円筒状隔膜10の上部10outに到達する。その間に処理水はアルカリイオンによりイオン化して、イオン水流出口パイプ接続部14cから流出する。   Water to be treated with alkaline ionized water is caused to flow from the treated water inlet pipe connecting portion 18a. This inflow water passes through the treated water flow pipe 18 and reaches the lower part 10 in of the cylindrical diaphragm 10. Here, the treated water rises between the cylindrical diaphragm 10 and the negative central electrode and reaches the upper part 10out of the cylindrical diaphragm 10. In the meantime, the treated water is ionized by alkali ions and flows out from the ion water outlet pipe connection part 14c.

次に、図3に本発明の第2の実施の形態を示す。単位となる電気分解ユニット20をn段並列に接続した多段型アルカリイオン水生成装置を示す。図3において第1段だけならば図1に示した第1実施例と同様な構成となる。   Next, FIG. 3 shows a second embodiment of the present invention. 1 shows a multi-stage alkaline ionized water generator in which unit electrolysis units 20 are connected in parallel in n stages. In FIG. 3, if only the first stage is used, the configuration is the same as that of the first embodiment shown in FIG.

多段用電解槽160は、その上部に図3に示すようにnヶ所の保持板受口部16aが設けられ、それぞれの受口部16aへ単位電気分解ユニット20を挿入して、固定ネジ19aによりネジ孔19bを通して電解槽160のネジ受16cへネジ止めする。   As shown in FIG. 3, the multi-stage electrolytic cell 160 is provided with n holding plate receiving portions 16a, and the unit electrolysis unit 20 is inserted into each receiving portion 16a and fixed by a fixing screw 19a. The screw hole 19b is screwed to the screw receiver 16c of the electrolytic cell 160.

n個の単位電気分解ユニット20をn段並列に動作させることにより、図1に示した1段で処理できる流入量のn倍の処理水を同一時間内に処理し、n倍のイオン水を流出させるものである。   By operating n unit electrolysis units 20 in n stages in parallel, treated water of an inflow amount that can be treated in one stage shown in FIG. 1 is treated in the same time, and n times of ionized water is treated. It is something to be drained.

図3に示す各単位電気分解ユニット20はすべて、それらのユニットの処理水入口パイプ接続部18aとイオン水流出口パイプ接続部14cとは配置方向が同一となるようにして、電解槽160の保持板受口部16aへ挿入されている。   The unit electrolysis unit 20 shown in FIG. 3 is such that the treated water inlet pipe connection portion 18a and the ionic water outlet pipe connection portion 14c of these units are arranged in the same direction, and the holding plate of the electrolytic cell 160 It is inserted into the receiving part 16a.

それらのパイプ接続部18a及び14cにはそれぞれ水流開閉コック30が接続され、n個のパイプ接続部18aはそれぞれ水流開閉コック30を介して処理水入口n個のパイプ接続部18aへ分岐する総処理水入口パイプ部180へ接続される。処理水入力は開閉コック180aを介して行われる。   A water flow opening / closing cock 30 is connected to each of the pipe connecting portions 18a and 14c, and each of the n pipe connecting portions 18a branches to the treated water inlet n pipe connecting portions 18a via the water flow opening / closing cock 30. Connected to the water inlet pipe section 180. The treated water is input through the open / close cock 180a.

一方、n個のイオン水流出口パイプ接続部14cはそれぞれ開閉コック30を介してイオン水出口n個のイオン水流出口パイプ接続部14cへ分岐する総アルカリイオン水出口パイプ部140へ接続される。イオン水流出は開閉コック140aを介して行われる。   On the other hand, the n ion water outlet pipe connection portions 14c are connected to the total alkaline ion water outlet pipe portion 140 branching to the ion water outlet n ion water outlet pipe connection portions 14c via the opening / closing cock 30, respectively. Ionized water is discharged through the open / close cock 140a.

なお、190はイオン水出口側の発生ガス回収口である。また、電解槽160の一方の側面下部には、電解質溶液17の汲上げ出力コック170aを設け、循環用ポンプPによりその汲上げ電解質溶液を戻す循環用入力コック170bが他方の側面上部に設けてある。   Reference numeral 190 denotes a generated gas recovery port on the ionic water outlet side. Further, a pumping output cock 170a for the electrolyte solution 17 is provided at the lower part of one side surface of the electrolytic cell 160, and a circulation input cock 170b for returning the pumped electrolyte solution by the circulation pump P is provided at the upper part of the other side surface. is there.

n段の単位電気分解ユニット20−1,20−2、20−3、・・・・20−(n−2),20−(n−1),20−nは、それぞれ一端側から順次処理水入口パイプ接続部18a、処理水流水パイプ部18、正電極12及びその端子12a、負電極11及びそのフランジ11b、端子11a及び円筒状隔膜10、アルカリイオン水流出口パイプ接続部14cが一列に配列されている。   The n-stage unit electrolysis units 20-1, 20-2, 20-3,... 20- (n-2), 20- (n-1), 20-n are sequentially processed from one end side. The water inlet pipe connecting portion 18a, the treated water flowing water pipe portion 18, the positive electrode 12 and its terminal 12a, the negative electrode 11 and its flange 11b, the terminal 11a and the cylindrical diaphragm 10, and the alkali ion water outlet pipe connecting portion 14c are arranged in a line. Has been.

この第2実施例のn段型アルカリイオン水生成装置は1段のみのアルカリイオン水生成装置に比べて単位時間当たりn倍の処理水処理を行うことができる。   The n-stage alkaline ionized water generator of the second embodiment can perform treated water treatment of n times per unit time as compared with a single-stage alkaline ionized water generator.

動作させる場合は各段のn個の正電極端子12aを接続して直流電源の+に接続する。一方各段の負電極端子11aを接続して直流電源の−に接続する。   When operating, n positive electrode terminals 12a of each stage are connected and connected to + of the DC power source. On the other hand, the negative electrode terminal 11a of each stage is connected and connected to-of the DC power source.

図4は、本発明の第3の実施の形態の複式多段型アルカリイオン水生成装置を示す。第1の電気分解ユニット200aと、そのユニット20内に接続されている各部材群の配置が反転している第2の電気分解ユニット200bとが図4に示すように直列に接続して第1段の複式ユニット200a+200bとする。この複式ユニット200a+200bをn段並列に接続し、複式多段型アルカリイオン水生成装置となる。つぎに、それらの接続について詳細に説明する。   FIG. 4 shows a dual multi-stage alkaline ionized water generator according to the third embodiment of the present invention. The first electrolysis unit 200a and the second electrolysis unit 200b in which the arrangement of each member group connected in the unit 20 is reversed are connected in series as shown in FIG. A duplex unit 200a + 200b is provided. The duplex units 200a + 200b are connected in parallel in n stages to form a duplex multi-stage alkaline ionized water generator. Next, these connections will be described in detail.

先ず、電気分解ユニット200aとその反転配置電気分解ユニット200bとをそれぞれの処理水入口パイプ接続部18aに水流の開閉コック30を接続し、それら開閉コック30を4方向接続フランジを介して接続する。これによって電気分解ユニット200aと電気分解ユニット200bが直列に接続される。   First, the electrolysis unit 200a and its inverted arrangement electrolysis unit 200b are connected to the treated water inlet pipe connecting portion 18a with a water flow open / close cock 30, and the open / close cock 30 is connected via a four-way connection flange. As a result, the electrolysis unit 200a and the electrolysis unit 200b are connected in series.

更に、前記4方向接続フランジを介して第1段から第n段まで、順次接続する。この一端は総処理水入口パイプ部180に接続され、さらに開閉コック180aを介して処理水入口に至る。なお、その間に3方向接続フランジがあり処理水量流量調節弁210が設けられている。   Further, the first to nth stages are sequentially connected through the four-way connection flange. This one end is connected to the total treated water inlet pipe section 180, and further reaches the treated water inlet via the open / close cock 180a. In addition, there is a three-way connecting flange between them, and a treated water flow rate adjusting valve 210 is provided.

一方、直列に接続されたユニット200aと200bのイオン水流出口パイプ接続部14cは、それぞれ水流の開閉コック30を接続し、電解槽160の両方の側面上部付近にあるパイプ支持台140b(図5参照)上にそれぞれn個のパイプ分岐管を有する総アルカリイオン水出口パイプ部140−1及び140−2のそれぞれの分岐部に両側それぞれn個ある開閉コック30を接続する。このとき、パイプ分岐管の代わりに3方向接続フランジを使用しても良い。   On the other hand, the ionic water outlet pipe connecting portions 14c of the units 200a and 200b connected in series are connected to the water flow opening / closing cocks 30, respectively, and are pipe support bases 140b (see FIG. 5) near the upper portions of both side surfaces of the electrolytic cell 160. ) N open / close cocks 30 on both sides are connected to the respective branch portions of the total alkali ion water outlet pipe portions 140-1 and 140-2 each having n pipe branch pipes thereon. At this time, a three-way connection flange may be used instead of the pipe branch pipe.

総アルカリイオン水出口パイプ部140−1及び140−2は、それぞれ開閉コック140aを介して1本のパイプに接続されアルカリイオン水出口へ通ずる。   The total alkali ion water outlet pipe portions 140-1 and 140-2 are connected to one pipe via the open / close cock 140a, respectively, and lead to the alkali ion water outlet.

170a、170bは図3と同様に電解質溶液17を循環させるための汲上げ出力コック、循環用入力コックである。   Reference numerals 170a and 170b denote pumping output cocks and circulation input cocks for circulating the electrolyte solution 17 as in FIG.

16bは、電解槽160のガス抜孔回収部である。190はイオン水出口側の発生ガス回収口である。   16 b is a gas vent recovery part of the electrolytic cell 160. Reference numeral 190 denotes a generated gas recovery port on the ionic water outlet side.

図5は、図4に示した複式多段型アルカリイオン水生成装置の電気分解ユニット200a及びその反転配置された第2の電気分解ユニット200bが連結する各段の状態を示す断面図である。   FIG. 5 is a cross-sectional view showing the state of each stage where the electrolysis unit 200a of the duplex multi-stage alkaline ionized water generator shown in FIG. 4 and the second electrolysis unit 200b arranged in an inverted manner are connected.

電気分解ユニット200a及び200bは、そのメンテナンス時には2枚のユニット保持板材19のそれぞれの固定ネジ19aを外し、上方へ吊り上げ、電解槽160より取り外し、保守(隔膜や電極の交換など)を行なう。   During the maintenance of the electrolysis units 200a and 200b, the fixing screws 19a of the two unit holding plate members 19 are removed, lifted upward, removed from the electrolytic cell 160, and maintenance (exchange of diaphragms and electrodes, etc.) is performed.

複式直列接続の各段は、その保守したい段の両端に接続する水流の開閉コック30を取り外せば、その段だけ上方へ吊上げることができる。   Each stage of the double series connection can be lifted upward by removing the water flow opening / closing cock 30 connected to both ends of the stage to be maintained.

第3の実施の形態の複式多段(n段)型アルカリイオン水生成装置と、第1の実施の形態を比較すれば、同一寸法の電気分解ユニット20を用いて、単位時間当たり2n倍の処理水をイオン化処理することができる。   Comparing the multi-stage (n-stage) type alkaline ionized water generating apparatus of the third embodiment with the first embodiment, using the electrolysis unit 20 of the same size, a process of 2n times per unit time Water can be ionized.

次に、本発明の第4の実施の形態の高密度用電気分解ユニット300をm行n列にm×n個配設したアルカリイオン水生成装置を図6及び図7に基き説明する。   Next, an alkaline ionized water generating device in which m × n electrolysis units 300 for high density according to a fourth embodiment of the present invention are arranged in m rows and n columns will be described with reference to FIGS. 6 and 7.

図6(a)は、高密度電気分解ユニット300の構造図である。高密度電気分解ユニット300は、円筒状隔膜10、その中心軸に配設した負の中心電極11、円筒状隔膜10の外側にリングスペーサ15を介して配設した陽の外円筒電極12からなる。また、以上の円筒状隔膜10、中心電極11、外円筒電極12の各電極の間隙距離11d、12dを所定長に維持し、一体化して高密度電気分解ユニット300を形成する為の上部接続部材300b、下部接続部材300cを設ける。この上下接続部材300b、cとリングスペーサ15により外円筒電極12と円筒状隔膜10が固定される。   FIG. 6A is a structural diagram of the high-density electrolysis unit 300. The high-density electrolysis unit 300 includes a cylindrical diaphragm 10, a negative central electrode 11 disposed on the central axis thereof, and a positive outer cylindrical electrode 12 disposed on the outside of the cylindrical diaphragm 10 via a ring spacer 15. . The upper connecting member for forming the high-density electrolysis unit 300 by maintaining the gap distances 11d and 12d of the cylindrical diaphragm 10, the center electrode 11, and the outer cylindrical electrode 12 at a predetermined length and integrating them. 300b and a lower connecting member 300c are provided. The outer cylindrical electrode 12 and the cylindrical diaphragm 10 are fixed by the upper and lower connecting members 300b and 300c and the ring spacer 15.

すなわち、上部接続部材300b、下部接続部材300cにはそれぞれ円筒溝300dが設けてある。この円筒溝300dの外側の溝壁径は外円筒電極12の外径に合わせ、円筒溝300dの内側の溝壁径は円筒状隔膜10の内径に合わせておく。以上のようにすればそれらの円筒溝300dに図6(a)に示すようにリングスペーサ15と外円筒電極12及び円筒状隔膜10を挿入して、上下の接続部材300b、300cにより一体化させることができる。   That is, the upper connecting member 300b and the lower connecting member 300c are provided with cylindrical grooves 300d, respectively. The outer groove wall diameter of the cylindrical groove 300d is matched with the outer diameter of the outer cylindrical electrode 12, and the inner groove wall diameter of the cylindrical groove 300d is matched with the inner diameter of the cylindrical diaphragm 10. If it carries out as mentioned above, as shown to Fig.6 (a), the ring spacer 15, the outer cylindrical electrode 12, and the cylindrical diaphragm 10 will be inserted in those cylindrical grooves 300d, and it will integrate with upper and lower connecting members 300b and 300c. be able to.

また、その上下の接続部材300b、300cの内周壁部300lに中心電極支持用羽根部材300aをそれぞれ挿入して固着する。それら羽根部材300aの中心孔へ中心電極11の両端を挿入して中心電極11を固定する。この羽根部材300aは処理水が流入、流出する間隙を有しているので、処理水の流れがスムーズに行われると同時に中心電極11を中心位置に固定する機能とを併せ持つ。   Further, the center electrode supporting blade member 300a is inserted into and fixed to the inner peripheral wall portions 300l of the upper and lower connecting members 300b and 300c. The center electrode 11 is fixed by inserting both ends of the center electrode 11 into the center holes of the blade members 300a. Since the blade member 300a has a gap through which treated water flows in and out, the blade member 300a has a function of fixing the center electrode 11 at the center position while the treated water flows smoothly.

さらに、その中心電極11と負の中心電極端子11aを外被絶縁管の導線で接続する。また、正の外円筒電極端子12aと外被絶縁管の導線で接続する。以上で高密度電気分解ユニット300の1単位とする固着された構造となる。   Furthermore, the center electrode 11 and the negative center electrode terminal 11a are connected by the conducting wire of the jacket insulation tube. In addition, the positive outer cylindrical electrode terminal 12a is connected to the outer insulating tube lead. With the above, a fixed structure as one unit of the high-density electrolysis unit 300 is obtained.

図6(b)は、図6(a)の高密度電気分解ユニット300をm行×n列に配設した高密度型のアルカリイオン水生成装置を示し、(b)には、m行に配設されたn個の高密度電気分解ユニット300の各中心軸を通る断面図と、電解槽360の上方から見た平面図とを示す。   FIG. 6B shows a high-density alkaline ionized water generating apparatus in which the high-density electrolysis units 300 of FIG. 6A are arranged in m rows × n columns, and FIG. 6B shows m rows. Sectional drawing which passes along each central axis of the n high-density electrolysis unit 300 arrange | positioned, and the top view seen from the upper direction of the electrolytic cell 360 are shown.

m×n個の高密度電気分解ユニット300は、電解槽360の底面に設けらたm×n個の孔にそれぞれ接続部材300cの先端を挿入し電解槽360中に固定し、反対側の接続部材300bをm×n個の孔を有する電解槽360の上面蓋に挿入するようにして高密度電気分解ユニット300をその上下の孔で固定する。   The m × n high-density electrolysis units 300 are inserted into m × n holes provided on the bottom surface of the electrolytic cell 360, the tips of the connection members 300 c are respectively inserted into the electrolytic cell 360, and fixed on the opposite side. The member 300b is inserted into the upper surface lid of the electrolytic cell 360 having m × n holes, and the high-density electrolysis unit 300 is fixed by the upper and lower holes.

また、処理水入口から開閉コックを介して総処理水入口パイプ180を経由して電解槽360の下側にある各高密度電気分解ユニット300の下部の接続部材300cへ接続させる。   Moreover, it connects with the connection member 300c of the lower part of each high-density electrolysis unit 300 in the lower side of the electrolytic cell 360 via the total treated water inlet pipe 180 from the treated water inlet via the open / close cock.

図では、第1列分岐管からm個の各ユニット300は処理水が入力され、・・・・第n列分岐管からm個の各ユニットへ処理水が分流する。   In the figure, treated water is input to each of the m units 300 from the first row branch pipe,..., The treated water is diverted from the nth row branch pipe to the m units.

一方、それぞれのm×n個の各ユニット300の下側から円筒状隔膜10に流入された処理水は、イオン化されながら上部の接続部材300bから流出し、第m行のn個の各ユニット300のイオン水が集められ総アルカリイオン水出口パイプ部140の第m行分岐管へ流出させ、・・・・第1行のn個の各ユニット300のイオン水が集められ総アルカリイオン水出口パイプ部140の第1行分岐管へ流出させ、全てのアルカリイオン水を出口パイプ部140に集めて流出させる。   On the other hand, the treated water flowing into the cylindrical diaphragm 10 from the lower side of each of the m × n units 300 flows out of the upper connection member 300b while being ionized, and the n units 300 in the m-th row. Ionic water is collected and allowed to flow out to the m-th branch branch pipe of the total alkaline ion water outlet pipe section 140... It is made to flow out to the 1st row branch pipe of part 140, and all alkali ion water is collected in outlet pipe part 140, and is made to flow out.

図7は、高密度電気分解ユニット300を4行3列に配設したときのアルカリイオン水生成装置を示す。すなわち、高密度電気分解ユニット300は12個使用し、その構成上小型でコンパクトな構造で、単位時間当たり大量の処理水をイオン化することができる。図7は斜視図で、その外観を示すが、その電解槽360を一点鎖線で示す。   FIG. 7 shows an alkaline ionized water generator when high-density electrolysis units 300 are arranged in 4 rows and 3 columns. That is, twelve high-density electrolysis units 300 are used, and a large amount of treated water per unit time can be ionized with a compact and compact structure in terms of its configuration. FIG. 7 is a perspective view showing the external appearance, and the electrolytic cell 360 is indicated by a one-dot chain line.

また、処理水入口から総処理水入口パイプ部180を経由して12個の高密度電気分解ユニット300へ分流させているが、その水流パイプは線で示してある。各高密度電気分解ユニット300への接続は12個の3方向接続フランジを用いる。   In addition, the water flow is divided into 12 high-density electrolysis units 300 from the treated water inlet via the total treated water inlet pipe section 180, and the water flow pipes are indicated by lines. The connection to each high-density electrolysis unit 300 uses 12 three-way connection flanges.

一方、12個の各高密度電気分解ユニット300の円筒状隔膜10中を通りイオン化して流出したイオン水は、それぞれ12個の3方向フランジを通して総アルカリイオン水出口パイプ部140に集められる。   On the other hand, the ionized water that is ionized and flows out through the cylindrical diaphragm 10 of each of the twelve high-density electrolysis units 300 is collected in the total alkaline ionized water outlet pipe section 140 through twelve three-way flanges.

各高密度電気分解ユニット300のメンテナンスにおいては、それぞれのユニット300の上下に接続されている3方向接続フランジのネジ止めを取れば容易にそのユニット300を電解槽360より取り出し、部品の点検交換等を行なえる。   For maintenance of each high-density electrolysis unit 300, if the three-way connecting flanges connected to the upper and lower sides of each unit 300 are screwed, the unit 300 can be easily taken out from the electrolytic cell 360, and parts can be inspected and replaced. Can be done.

図1〜図7については外円筒電極12を陽電極として、中心電極を負電極として、円筒状隔膜10の円筒内に処理水を流せばアルカリイオン水として生成する装置を述べたが、これらの外円筒電極12を負電極とし、中心電極11を陽電極として動作させ円筒状隔膜10の円筒内に処理水を流入させれば強酸性イオン水を生成させることができる。すなわち、単位時間当たり大量の強酸性イオン水を生成させる酸性イオン水生成装置となる。   1 to 7, the outer cylindrical electrode 12 is used as a positive electrode, the central electrode is used as a negative electrode, and an apparatus that generates alkaline ionized water by flowing treated water into the cylinder of the cylindrical diaphragm 10 has been described. If the outer cylindrical electrode 12 is operated as a negative electrode and the central electrode 11 is operated as a positive electrode and treated water flows into the cylinder of the cylindrical diaphragm 10, strong acidic ionized water can be generated. That is, it becomes an acidic ionic water production | generation apparatus which produces | generates a large amount of strong acidic ionic water per unit time.

本発明の電気分解用セラミック隔膜を用いれば、電気分解による強アルカリイオン水或いは強酸性水の製造に加えて、電気分解による脱燐、脱窒素、重金属分離、Ph調整などの工業用排水・廃液処理、坑道廃水処理、冷却塔循環水の水質維持装置として多様な形状、容積(小型化)で利用することができる。   If the ceramic diaphragm for electrolysis of the present invention is used, in addition to the production of strong alkaline ionized water or strong acid water by electrolysis, industrial wastewater and waste liquids such as dephosphorization, denitrification, heavy metal separation, and Ph adjustment by electrolysis It can be used in various shapes and volumes (downsizing) as a water quality maintenance device for treatment, mine wastewater treatment, and cooling tower circulating water.

本発明の第1の実施の形態のアルカリイオン水生成装置の構造を示し、(a)は断面図、(B)は平面図である。The structure of the alkaline ionized water production | generation apparatus of the 1st Embodiment of this invention is shown, (a) is sectional drawing, (B) is a top view. アルカリイオン水生成装置のユニット取り出し状態の説明図である。It is explanatory drawing of the unit taking-out state of an alkaline ionized water production | generation apparatus. 本発明の第2の実施の形態の多段型アルカリイオン水生成装置の構造を示す平面図である。It is a top view which shows the structure of the multistage type | mold alkaline ionized water production | generation apparatus of the 2nd Embodiment of this invention. 本発明の第3の実施の形態の複式多段型アルカリイオン水生成装置の構造を示す平面図である。It is a top view which shows the structure of the duplex multistage type | mold alkaline ionized water production | generation apparatus of the 3rd Embodiment of this invention. 図4の複式多段型アルカリイオン水生成装置の断面図である。FIG. 5 is a cross-sectional view of the dual multi-stage alkaline ionized water generator of FIG. 4. 本発明の第4の実施の形態の高密度陽電気分解ユニットを配列したアルカリイオン水生成装置を示し、(a)はユニットの断面図、(b)は装置の断面図、(c)は装置の平面図である。The alkaline ionized water production | generation apparatus which arranged the high-density positive electrolysis unit of the 4th Embodiment of this invention is shown, (a) is sectional drawing of a unit, (b) is sectional drawing of an apparatus, (c) is apparatus FIG. 本発明の第4の実施の形態のアルカリイオン水生成装置の構造を示す斜視図である。It is a perspective view which shows the structure of the alkaline ionized water production | generation apparatus of the 4th Embodiment of this invention.

符号の説明Explanation of symbols

10 円筒状隔膜(イオン交換隔膜)
10in 処理水隔膜入口
10out イオン水隔膜出口
11 中心電極
11a 中心電極端子
11b 中心電極端子板
11d 間隙距離
12 外円筒電極
12a 外円筒電極端子
12d 間隙距離
13 下部接続部材
13a フランジ
13b 上下部パイプ
14 上部接続部材
14a パイプ
14b 中心電極端子接続用フランジ
14c イオン水流出口パイプ接続部
15 リングスペーサ
16 電解槽
16a 保持板受口部
16b ガス抜孔回収部
16c ネジ受
17 電解質溶液
17a 溶液水位
18 処理水流出パイプ
18a 処理水入口パイプ接続部
19 ユニット保持板材
19a 固定ネジ
19b ネジ孔
20 単位電気分解ユニット
20−1,20−n 第1段ユニット〜第n段ユニット
21 補強アングル材
22 圧縮空気入力用パイプ端子
22a 空気入力口
30 開閉コック
140、140−1,n 総アルカリイオン水出口パイプ部
140a 開閉コック
140b パイプ支持台
160 電解槽(多段用)
170a 汲上げ出力コック
170b 循環用入力コック
180 総処理水入口パイプ部
180a 開閉コック
190 発生ガス回収口
200a 第1の電気分解ユニット
200b 第2の電気分解ユニット
210 処理水流量調整弁
300 高密度用電気分解ユニット
300a 中心電極支持用羽根部材
300b 上部接続部材
300c 下部接続部材
300d 円筒溝
300e 内周壁部
360 高密度用電解槽
10 Cylindrical diaphragm (ion exchange diaphragm)
10in treated water diaphragm inlet 10out ion water diaphragm outlet 11 central electrode 11a central electrode terminal 11b central electrode terminal plate 11d gap distance 12 outer cylindrical electrode 12a outer cylindrical electrode terminal 12d gap distance 13 lower connecting member 13a flange 13b upper and lower pipe 14 upper connection Member 14a Pipe 14b Center electrode terminal connecting flange 14c Ion water outlet pipe connecting part 15 Ring spacer 16 Electrolytic tank 16a Holding plate receiving part 16b Gas vent recovery part 16c Screw receiving 17 Electrolyte solution 17a Solution water level 18 Treated water outflow pipe 18a Treatment Water inlet pipe connection portion 19 Unit holding plate material 19a Fixing screw 19b Screw hole 20 Unit electrolysis unit 20-1, 20-n First stage unit to nth stage unit 21 Reinforcing angle member 22 Pipe terminal 22a for compressed air input Air input port 30 Open / close cock 140, 140-1, n Total alkali ion water outlet pipe 140a Open / close cock 140b Pipe support 160 Electrolyzer (for multistage)
170a Pumping output cock 170b Circulating input cock 180 Total treated water inlet pipe section 180a Opening / closing cock 190 Generated gas recovery port 200a First electrolysis unit 200b Second electrolysis unit 210 Treated water flow rate adjustment valve 300 High density electricity Disassembly unit 300a Center electrode supporting blade member 300b Upper connection member 300c Lower connection member 300d Cylindrical groove 300e Inner peripheral wall 360 High-density electrolytic cell

Claims (7)

棒状又はパイプ状の負の中心電極の中心軸に円筒型に成形されたイオン交換隔膜の中心軸を合わせて所定の間隙距離を維持して配設し、
その円筒状隔膜の外側に円筒型に成形されたメッシュ状又は電解溶液透過性の正の外側筒電極の中心軸を合わせて所定の間隙距離を維持して配設し、
前記円筒状隔膜の外側では電解質溶液を循環させ、その隔壁の内側では下部より処理水を流入させて、前記正・負電極間に直流電圧を印加して、電気分解を行わせ、隔壁上部より処理水をアルカリイオン化して流出させるアルカリイオン水生成装置であって、
前記隔膜は、最大長が0.5〜2mm径の範囲に入る粒状或いは破砕された結晶性粘土鉱物を主体としたセラミックに対し、85〜95℃に加熱した水溶性高分子材を10〜30重量%混入して混練し、補強用布状繊維上に圧出成形して平板成形材とし、直後に円筒状の型材に捲き付けて乾燥させた、円筒状のセラミック混入樹脂バインダー層からなる隔膜構造を備え、
その隔膜の下部には、そのフランジから上下方向にそれぞれ所定長のパイプを有し、そのパイプの外径は、前記隔膜の内径に合わせ、上側パイプは隔膜下端円周内側に接続可能とし、下側パイプは前記処理水の流入パイプの内側に接続可能とする下部接続部材を備え、
前記隔膜の上部には、外径が前記隔膜内径に合わせたパイプを有し、そのパイプ下側と隔膜上端円周内側に接続可能とし、そのパイプ上側端部は前記負の中心電極端子接続用フランジを有し、さらに処理水のアルカリイオン水流出口パイプ接続部とを有する上部接続部材を備え、
前記隔膜円筒部外側には、前記正の外円筒電極が前記所定の間隙距離を維持するための隔膜の外側の上下端2ヶ所に嵌められた電気絶縁性のリングスペーサを備え、
前記隔膜の外側まで前記正の外円筒電極を透過して電解質溶液を循環させる為の電解質溶液を収容する電解槽を備え、
前記上部接続部材のパイプ中間部には、その上部接続部材と、その上側でフランジにより連結する負の中心電極端子板および負の中心電極端子と、上部接続部材の下側にフランジとスペーサにより連結する隔膜及び正の外円筒電極と、前記隔膜の下端部に下部接続部材を介して連結する処理水流入パイプと、それを連結する処理水入口パイプ接続部とを接続した電気分解ユニットをそのまま保持する状態で溶着されたユニット保持板材を備え、
前記電解槽の上部には、前記保持部材に保持された、前記電気分解ユニットを装着したまま、その電解槽の上側から挿入して電気分解ユニットを電解質溶液に沈めて、前記保持板材の周縁を電解槽の上側に載せてネジ留できる保持板材受口部と、前記電解質溶液から発生する外円筒極側ガス抜き孔部とを備えることを特徴とするアルカリイオン水生成装置。
Aligning the central axis of the cylindrical ion-exchange membrane with the central axis of the rod-shaped or pipe-shaped negative central electrode, maintaining a predetermined gap distance,
Maintaining a predetermined gap distance by aligning the central axis of the mesh-shaped or electrolytic solution-permeable positive outer cylinder electrode formed in a cylindrical shape outside the cylindrical diaphragm,
The electrolyte solution is circulated outside the cylindrical diaphragm, the treated water is allowed to flow from the bottom inside the partition, and a DC voltage is applied between the positive and negative electrodes to perform electrolysis, from above the partition. An alkaline ionized water generating apparatus for alkalinely ionizing treated water to flow out,
The diaphragm is made of 10-30 water-soluble polymer material heated to 85-95 ° C with respect to a ceramic mainly composed of granular or crushed crystalline clay mineral having a maximum length of 0.5-2 mm. A diaphragm composed of a cylindrical ceramic-mixed resin binder layer mixed and kneaded by weight, extruded onto a reinforcing fabric fiber to form a flat plate molding material, and immediately spread on a cylindrical mold material and dried. With structure,
The lower part of the diaphragm has pipes each having a predetermined length in the vertical direction from the flange. The outer diameter of the pipe matches the inner diameter of the diaphragm, and the upper pipe can be connected to the inner circumference of the lower end of the diaphragm. The side pipe includes a lower connection member that can be connected to the inside of the treated water inflow pipe,
The upper part of the diaphragm has a pipe whose outer diameter matches the inner diameter of the diaphragm, and can be connected to the lower side of the pipe and the inner circumference of the upper end of the diaphragm, and the upper end of the pipe is used for connecting the negative central electrode terminal. An upper connection member having a flange and further having an alkali ion water outlet pipe connection part of the treated water;
Outside the diaphragm cylindrical portion, the positive outer cylindrical electrode is provided with electrically insulating ring spacers fitted at two upper and lower ends on the outer side of the diaphragm for maintaining the predetermined gap distance,
An electrolytic cell containing an electrolyte solution for circulating the electrolyte solution through the positive outer cylindrical electrode to the outside of the diaphragm;
Connected to the pipe intermediate part of the upper connecting member by the upper connecting member, the negative central electrode terminal plate and the negative central electrode terminal connected by the flange on the upper side, and the flange and spacer on the lower side of the upper connecting member The electrolysis unit that holds the diaphragm and the positive outer cylindrical electrode, the treated water inflow pipe connected to the lower end of the diaphragm via the lower connecting member, and the treated water inlet pipe connecting part for holding it is held as it is. Unit holding plate material welded in a state to
With the electrolysis unit held by the holding member attached to the upper part of the electrolytic cell, the electrolysis unit is inserted from the upper side of the electrolytic cell and the electrolysis unit is submerged in the electrolyte solution, so that the periphery of the holding plate is An alkaline ionized water generating apparatus comprising: a holding plate member receiving portion that can be screwed on the upper side of an electrolytic cell; and an outer cylindrical pole side gas vent hole portion generated from the electrolyte solution.
前記処理水流入パイプには、堆積物をエアリフトさせる圧縮空気入力用パイプ端子を備えることを特徴とする請求項1記載のアルカリイオン水生成装置。   The alkaline ionized water generating apparatus according to claim 1, wherein the treated water inflow pipe includes a compressed air input pipe terminal for air-lifting the deposit. 前記電解層の横方向に沿って一端側から順次前記処理水パイプ接続部、処理水流水パイプ及び正電極(端子)、負電極(端子)及び隔膜、アルカリイオン水流出口パイプ接続部が一列に配列される構造の単位電気分解ユニットを備えて、
その電解槽の奥行方向に沿って、前記単位電気分解ユニットをn段配設できるように、前記電解槽の上部にnヶ所の前記保持板材受口部を備え、
各単位電気分解ユニットの前記処理水入り口部に接続し、n段分の処理水を流入させる総処理水入口パイプ部と、
各単位電気分解ユニットの前記アルカリイオン水流出口部に接続し、n段分のアルカリイオン水を流出させる総アルカリイオン水出口パイプ部とを備え、
n段の単位電気分解ユニットを並列に動作させることを特徴とする請求項1又は2に記載のアルカリイオン水生成装置。
The treated water pipe connection part, the treated water running water pipe and the positive electrode (terminal), the negative electrode (terminal) and the diaphragm, and the alkaline ionized water outlet pipe connecting part are arranged in a row from one end side along the lateral direction of the electrolytic layer. With unit electrolysis unit,
Along with the depth direction of the electrolytic cell, the unit electrolysis unit is provided with n holding plate material receiving portions at the upper part of the electrolytic cell so that the unit electrolysis unit can be arranged in n stages,
Connected to the treated water inlet part of each unit electrolysis unit, a total treated water inlet pipe part into which treated water for n stages flows,
It is connected to the alkaline ion water outlet part of each unit electrolysis unit, and comprises a total alkaline ion water outlet pipe part for allowing n stages of alkaline ion water to flow out,
The alkaline ionized water generating apparatus according to claim 1 or 2, wherein n unit electrolysis units are operated in parallel.
前記電解槽の第n段目の単位電気分解ユニットに近い位置から電解質溶液をポンプで汲み上げ、第1段目の単位電気分解ユニットに近い位置へ、その電解質溶液を循環させる循環パイプを備えることを特徴とする請求項3記載のアルカリイオン水生成装置。   A circulation pipe for pumping the electrolyte solution from a position near the n-th stage unit electrolysis unit of the electrolytic cell and circulating the electrolyte solution to a position near the first stage unit electrolysis unit; The alkaline ionized water generator according to claim 3, wherein 前記電解槽の横方向に沿って、一端側から順次前記アルカリイオン水流出口部、イオン水流出パイプ、負の中心電極(端子)及び正電極(端子)、処理水入口部が一列に配列される構造の第1の単位電気分解ユニットと、さらに、前記単位電気分解ユニットに順次接続する前記処理水入口部、正電極(端子)、負電極(端子)及び隔膜、アルカリイオン水出口部、イオン水流出パイプ部が一列に配列される反転構造の第2の単位電気分解ユニットを備え、
その電解槽の奥行方向に沿って直列に接続した前記第1及び第2の単位電気分解ユニットをn段配設できるように前記電解槽の上部には横方向に2ヶ所の前記保持板材受口部を奥行き方向にn段、合計n×2ヶ所備え、
第1の単位電気分解ユニットの前記アルカリイオン水流出部に接続し、n段分の処理水を流入させる横方向一端側に配設する第1のイオン水パイプ入口部と、
第2の単位電気分解ユニットの前記アルカリイオン水流出部に接続し、n段分の処理水を流入させる横方向他端側に配設する第2のイオン水パイプ入口部と、
第1及び第2の単位電気分解ユニットの前記処理水流出口部に接続し、n段×2個のアルカリイオン水を流出させる総処理水出口パイプ部とを備え、
n段×2個の単位電気分解ユニットを、2個直列n段並列に動作させることを特徴とする請求項1又は2に記載のアルカリイオン水生成装置。
The alkaline ion water outlet, ion water outlet pipe, negative central electrode (terminal) and positive electrode (terminal), and treated water inlet are arranged in a row in sequence from one end side along the lateral direction of the electrolytic cell. A first unit electrolysis unit having a structure; and the treated water inlet, a positive electrode (terminal), a negative electrode (terminal) and a diaphragm, which are sequentially connected to the unit electrolysis unit, an alkaline ion water outlet, and ionic water A second unit electrolysis unit having an inverted structure in which the outflow pipe portions are arranged in a line;
Two holding plate material receiving ports in the lateral direction are provided above the electrolytic cell so that n stages of the first and second unit electrolysis units connected in series along the depth direction of the electrolytic cell can be arranged. There are n stages in the depth direction, a total of nx 2 locations,
A first ionic water pipe inlet connected to the alkaline ionized water outflow part of the first unit electrolysis unit and disposed on one side in the lateral direction to allow treatment water for n stages to flow;
A second ionic water pipe inlet connected to the alkaline ion water outflow part of the second unit electrolysis unit and disposed on the other side in the lateral direction through which treated water for n stages flows.
Connected to the treated water outlet of the first and second unit electrolysis units, and comprises a total treated water outlet pipe for allowing n stages × 2 pieces of alkaline ionized water to flow out,
The alkaline ionized water generating apparatus according to claim 1 or 2, wherein two unit electrolysis units of n stages x 2 are operated in series and n stages in parallel.
棒状又はパイプ状の負の中心電極の中心軸に円筒型に成形されたイオン交換隔膜の中心軸を合わせて所定の間隙距離を維持して配設し、
その円筒状隔膜の外側に円筒型に成形されたメッシュ状又は電解溶液透過性の正の外円筒電極の中心軸を合わせて所定の間隙距離を維持して配設し、
前記円筒状隔膜の外側には電解質溶液を循環させ、その隔壁の内側には処理水を流入させて、前記正・負電極間に電圧を印加して、電気分解を行わせ、処理水をアルカリイオン化して流出させるアルカリイオン水生成装置であって、
前記隔膜は、0.5〜2mm径の粒状或いは破砕された結晶性粘土鉱物を主体としたセラミックに対し、85〜95℃に加熱した水溶性高分子材を10〜30重量%に混入して混練し、補強用布状繊維上に圧出成形して平板成形材とし、直後に円筒状の型材に捲き付けて乾燥させた、円筒状のセラミック混入樹脂バインダー層からなる隔膜構造を備え、
その隔膜の下部には、そのフランジから上下方向にそれぞれ所定長のパイプを有し、そのパイプの外径は、前記隔膜の内径に合わせ、上側パイプは隔膜下端円周内側に接続可能とし、下側パイプは前記処理水流入パイプの内側に接続可能とする下部接続部材を備え、
前記隔膜の上部には、外径が前記隔膜内径に合わせたパイプを有し、そのパイプ下側と隔膜上端円周内側に接続可能とし、そのパイプ上側端部は前記負電極端子接続用フランジを有し、さらに処理水のアルカリイオン水流出口を有する上部接続部材を備え、
前記隔膜円筒部外側には、前記正電極が前記所定の間隙距離を維持するための隔膜の外側の上下端2ヶ所に嵌められた電気絶縁性のリングスペーサを備え、
前記上部接続部材と、その上側でフランジにより連結する負電極端子板及び負電極と、上部接続部材の下側に連結する隔膜及び正電極と、前記隔膜の下端部に下部接続部材を介して連結する処理水流入パイプと、それに連結する処理水入力部とを接続した高密度用電気分解ユニットを備え、
その電気分解ユニットを横方向にm列、奥行き方向にn列、m×n個の行列に電解に配設し、
各電気分解ユニットの上部のアルカリイオン水流出口m×n個を総合する総合アルカリイオン水流出口パイプと、
各電気分解ユニットの下部の処理水入口m×n個を総合する総合処理水流入口パイプと、
各電気分解ユニットの負電極m×n個を接続した負電極端子と、
各電気分解ユニットの正電極m×n個を接続した正電極端子とを備えることを特徴とするアルカリイオン水生成装置。
Aligning the central axis of the cylindrical ion-exchange membrane with the central axis of the rod-shaped or pipe-shaped negative central electrode, maintaining a predetermined gap distance,
A mesh-shaped or electrolytic solution-permeable positive outer cylindrical electrode formed in a cylindrical shape outside the cylindrical diaphragm is aligned with the central axis of the positive diaphragm electrode to maintain a predetermined gap distance,
An electrolyte solution is circulated outside the cylindrical diaphragm, and treated water is allowed to flow inside the partition wall. A voltage is applied between the positive and negative electrodes to cause electrolysis, and the treated water is alkalinized. An alkaline ionized water generator that ionizes and flows out,
The diaphragm is made by mixing 10 to 30% by weight of a water-soluble polymer material heated to 85 to 95 ° C. with respect to a ceramic mainly composed of 0.5 to 2 mm diameter granular or crushed crystalline clay mineral. Kneaded, extruded on a reinforcing cloth-like fiber to form a flat plate molding material, and immediately after being spread on a cylindrical mold material and dried, comprising a diaphragm structure composed of a cylindrical ceramic-mixed resin binder layer,
The lower part of the diaphragm has pipes each having a predetermined length in the vertical direction from the flange. The outer diameter of the pipe matches the inner diameter of the diaphragm, and the upper pipe can be connected to the inner circumference of the lower end of the diaphragm. The side pipe includes a lower connection member that can be connected to the inside of the treated water inflow pipe,
The upper part of the diaphragm has a pipe whose outer diameter matches the inner diameter of the diaphragm, and can be connected to the lower side of the pipe and the inner circumference of the upper end of the diaphragm, and the upper end of the pipe has the flange for connecting the negative electrode terminal. Further comprising an upper connecting member having an alkaline ion water outlet for the treated water,
Outside the diaphragm cylindrical portion, the positive electrode is provided with electrically insulating ring spacers fitted at two upper and lower ends on the outer side of the diaphragm for maintaining the predetermined gap distance,
The upper connection member, a negative electrode terminal plate and a negative electrode connected by a flange on the upper side, a diaphragm and a positive electrode connected to the lower side of the upper connection member, and a lower connection part connected to a lower end portion of the diaphragm A high-density electrolysis unit that connects a treated water inflow pipe and a treated water input connected to the treated water inflow pipe,
The electrolysis unit is arranged for electrolysis in m columns in the horizontal direction, n columns in the depth direction, and m × n matrix,
A total alkali ion water outlet pipe that combines m × n alkali ion water outlets at the top of each electrolysis unit;
An integrated treated water inlet pipe that synthesizes m × n treated water inlets at the bottom of each electrolysis unit;
A negative electrode terminal connecting m × n negative electrodes of each electrolysis unit;
An alkaline ionized water generating apparatus comprising: a positive electrode terminal connected to m × n positive electrodes of each electrolysis unit.
請求項1、3、5、6のいずれか1項に記載のアルカリイオン水生成装置において、正・負電極端子を逆電極に接続することにより、処理水を酸性イオン化して、アルカリ水流出口部に酸性イオン水を生成することを特徴とする酸性イオン水生成装置。 The alkaline ionized water generating apparatus according to any one of claims 1, 3, 5, and 6, wherein the treated water is acidic ionized by connecting the positive and negative electrode terminals to the reverse electrode, and the alkaline water outlet part An acidic ion water generating device characterized by generating acidic ion water.
JP2003421699A 2003-12-18 2003-12-18 Alkaline ion water generator and acidic ion water generator Expired - Fee Related JP3965491B2 (en)

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