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JP6410619B2 - Pure water purification equipment - Google Patents
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JP6410619B2 - Pure water purification equipment - Google Patents

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JP6410619B2
JP6410619B2 JP2015009806A JP2015009806A JP6410619B2 JP 6410619 B2 JP6410619 B2 JP 6410619B2 JP 2015009806 A JP2015009806 A JP 2015009806A JP 2015009806 A JP2015009806 A JP 2015009806A JP 6410619 B2 JP6410619 B2 JP 6410619B2
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ion exchange
pure water
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water
fresh water
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正喜 内田
正喜 内田
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Disco Corp
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Description

本発明は、純水精製装置の特にイオン交換樹脂容器に関する。   The present invention relates to a pure water purifier, particularly an ion exchange resin container.

半導体デバイス製造工程で用いられる純水は、水道水等と比較して、不純物が限界近くまで除去されたものであり、フィルタ等である程度の不純物が除去された清水からイオン交換手段によってイオン分の除去が行われるのが通常である。半導体ウエーハ等を切削して分割する切削装置でも純水が用いられ、切削装置から排出される加工水から切削屑及び各種イオンを除去して再び切削装置に供給される純水精製装置の一種である加工廃液処理装置にもイオン交換手段が用いられる(例えば、特許文献1参照)。   The pure water used in the semiconductor device manufacturing process is one in which impurities have been removed to near the limit compared to tap water, etc., and the ion content from the fresh water from which some impurities have been removed by a filter or the like by ion exchange means. Removal is usually done. Pure water is also used in cutting devices that cut and divide semiconductor wafers, etc., and is a type of pure water purification device that removes cutting debris and various ions from the processing water discharged from the cutting device and supplies the cutting device again. An ion exchange means is also used in a processing waste liquid treatment apparatus (see, for example, Patent Document 1).

これらの装置のイオン交換手段は、ガラス繊維等で耐圧強化されている樹脂性の硬質な容器にイオン交換樹脂を収容し、その容器のイオン交換樹脂に清水を通すことでイオン分を除去し純水に精製している。硬質な容器はその構造が複雑であるため高価で重量が重く、交換にはコストと工数がかかるという課題があった。そこで、安価で軽い単層樹脂製の容器を用いる事を可能とした純水精製装置を本願発明者は発案した。   The ion exchange means of these devices is to remove the ion content by storing the ion exchange resin in a resinous hard container reinforced with glass fiber or the like and passing clean water through the ion exchange resin in the container. Purified into water. Since the structure of the hard container is complicated, it is expensive and heavy, and there is a problem that replacement requires cost and man-hours. Therefore, the inventor of the present application has devised a pure water purifying apparatus that makes it possible to use an inexpensive and light single-layer resin container.

特許第5086123号公報Japanese Patent No. 5086123

純水精製装置は、例えば切削装置に接続される場合、切削装置が稼働を停止していると純水精製装置に供給される水も停止される。この場合、容器の下方から清水を供給し上方から純水を排出する容器の形式では、容器内の空気は容器外に排出されやすいが、水の流れに沿ってイオン交換樹脂が容器内で上方に溜まり易く、清水の供給が停止すると、上方に溜まったイオン交換樹脂が容器の底部に向かって落ちてくるという現象が発生する。更にこの現象は、イオン交換樹脂がイオン分を吸着すると樹脂自体の体積も収縮し、容器内の空間が増えるためより顕著となる。この際、イオン交換樹脂として所定の混合比で混合されたカチオン樹脂(強酸性陽イオン交換樹脂)とアニオン樹脂(強塩基性陰イオン交換樹脂)とがその比重比差によって分級してしまい(参考:カチオン樹脂の方が比重が大きい)、イオン交換の効果が充分発揮できないという課題があった。   When the pure water purification apparatus is connected to, for example, a cutting apparatus, if the cutting apparatus stops operating, water supplied to the pure water purification apparatus is also stopped. In this case, in the container type in which fresh water is supplied from the lower side of the container and pure water is discharged from the upper side, the air in the container is easily discharged to the outside of the container, but the ion exchange resin moves upward in the container along the flow of water. When the supply of fresh water is stopped, the ion exchange resin accumulated above falls toward the bottom of the container. Furthermore, this phenomenon becomes more prominent because the volume of the resin itself shrinks when the ion exchange resin adsorbs ions, and the space in the container increases. At this time, the cation resin (strongly acidic cation exchange resin) and the anion resin (strongly basic anion exchange resin) mixed at a predetermined mixing ratio as the ion exchange resin are classified by the specific gravity ratio difference (reference) : The specific gravity of the cationic resin is larger), and there is a problem that the effect of ion exchange cannot be sufficiently exhibited.

本発明は、上記問題にかんがみなされたもので、その目的は、イオン交換の効果を充分に発揮することができる純水精製装置を提供することである。   The present invention has been considered in view of the above problems, and an object of the present invention is to provide a pure water purifier capable of sufficiently exhibiting the effect of ion exchange.

上述した課題を解決し、目的を達成するために、本発明の純水精製装置は、送水される清水を純水に精製するイオン交換手段と、該イオン交換手段によって精製された純水を該イオン交換手段から送出する送出手段と、を備える純水精製装置であって、該イオン交換手段は、イオン交換樹脂と流入口を備える天井部と、送出口を備える底部と、該天井部と該底部とを連結する側部とを有し、該イオン交換樹脂を収容する容器と、から構成され、上方の流入口から該清水が該容器に供給され、該容器は、該清水を供給する配管を該流入口に接続する接続手段を備え、該接続手段は、該配管と連結し、該配管を該流入口に固定する連結固定部と、該容器に挿入され、該清水を該容器に供給する導入管部を備え、該導入管部は、底部が広い円錐台形状で、傾斜した側部に噴出口が周方向沿って形成され、該底部が邪魔板となり、該導入管部の該噴出口から供給される該清水は、該噴出口から放射状に噴出することを特徴とする。 In order to solve the above-described problems and achieve the object, the pure water purifying apparatus of the present invention comprises ion exchange means for purifying fresh water to be supplied into pure water, and pure water purified by the ion exchange means. A deionized water purification apparatus comprising: a delivery means for delivering from an ion exchange means, wherein the ion exchange means comprises: a ceiling part comprising an ion exchange resin and an inlet; a bottom comprising a delivery outlet; the ceiling part; And a container for containing the ion exchange resin, and the fresh water is supplied from the upper inlet to the container, and the container is a pipe for supplying the fresh water. Connecting means for connecting the pipe to the inlet, the connecting means being connected to the pipe, a connecting and fixing portion for fixing the pipe to the inlet, and being inserted into the container to supply the fresh water to the container The introduction pipe part has a frustoconical shape with a wide bottom part. In, spout the inclined sides are formed along the circumferential direction, said bottom becomes baffles該清water supplied from該噴outlet of the introduction pipe portion, that ejected radially from該噴outlet Features.

そこで、本願発明の純水精製装置では、イオン交換手段を、所謂ダウンフローで清水を通水する構成としたため、イオン交換の効果を充分に発揮することができる、という効果を奏する。   Therefore, in the pure water purifying apparatus of the present invention, since the ion exchange means is configured to pass clear water by so-called downflow, there is an effect that the effect of ion exchange can be sufficiently exhibited.

図1は、実施形態に係る純水精製装置と隣接される加工装置としての切削装置の構成例を示す斜視図である。FIG. 1 is a perspective view illustrating a configuration example of a cutting device as a processing device adjacent to a pure water purification device according to an embodiment. 図2は、実施形態に係る純水精製装置の構成例を分解して示す分解斜視図である。FIG. 2 is an exploded perspective view showing an exploded configuration example of the pure water purifying apparatus according to the embodiment. 図3は、実施形態に係る純水精製装置のイオン交換手段を示す側断面図である。FIG. 3 is a side sectional view showing the ion exchange means of the pure water purifying apparatus according to the embodiment. 図4は、実施形態に係る純水精製装置のイオン交換手段の接続部材を示す図である。FIG. 4 is a diagram illustrating a connection member of the ion exchange means of the pure water purification apparatus according to the embodiment. 図5は、実施形態の変形例に係る純水精製装置のイオン交換手段の接続部材を示す図である。FIG. 5 is a diagram illustrating a connection member of an ion exchange unit of a pure water purifier according to a modification of the embodiment.

本発明を実施するための形態(実施形態)につき、図面を参照しつつ詳細に説明する。以下の実施形態に記載した内容により本発明が限定されるものではない。また、以下に記載した構成要素には、当業者が容易に想定できるもの、実質的に同一のものが含まれる。さらに、以下に記載した構成は適宜組み合わせることが可能である。また、本発明の要旨を逸脱しない範囲で構成の種々の省略、置換又は変更を行うことができる。   DESCRIPTION OF EMBODIMENTS Embodiments (embodiments) for carrying out the present invention will be described in detail with reference to the drawings. The present invention is not limited by the contents described in the following embodiments. The constituent elements described below include those that can be easily assumed by those skilled in the art and those that are substantially the same. Furthermore, the structures described below can be combined as appropriate. Various omissions, substitutions, or changes in the configuration can be made without departing from the scope of the present invention.

〔実施形態〕
本発明の実施形態に係る純水精製装置を図面に基いて説明する。図1は、実施形態に係る純水精製装置と隣接される加工装置としての切削装置の構成例を示す斜視図である。図2は、実施形態に係る純水精製装置の構成例を分解して示す分解斜視図である。図3は、実施形態に係る純水精製装置のイオン交換手段を示す側断面図である。図4(a)は、実施形態に係る純水精製装置のイオン交換手段の接続部材を示す側部図である。図4(b)は、実施形態に係る純水精製装置のイオン交換手段の接続部材を示す上面図である。
Embodiment
A pure water purifier according to an embodiment of the present invention will be described with reference to the drawings. FIG. 1 is a perspective view illustrating a configuration example of a cutting device as a processing device adjacent to a pure water purification device according to an embodiment. FIG. 2 is an exploded perspective view showing an exploded configuration example of the pure water purifying apparatus according to the embodiment. FIG. 3 is a side sectional view showing the ion exchange means of the pure water purifying apparatus according to the embodiment. Fig.4 (a) is a side view which shows the connection member of the ion exchange means of the pure water refiner | purifier which concerns on embodiment. FIG.4 (b) is a top view which shows the connection member of the ion exchange means of the pure water refiner | purifier which concerns on embodiment.

実施形態に係る純水精製装置1は、図1に示す加工装置としての切削装置100に隣接されて配置される。切削装置100は、図1に示すように、被加工物Wを保持するチャックテーブル110と、チャックテーブル110に保持された被加工物Wを切削するための切削ブレード121と切削ブレード121に切削水を供給する切削供給ノズル122とを備えた切削手段120と、チャックテーブル110をX軸方向に移動させるX軸移動手段(図示せず)と、切削手段120をY軸方向に移動させるY軸移動手段(図示せず)と、切削手段120をZ軸方向に移動させるZ軸移動手段(図示せず)と、チャックテーブル110をZ軸と平行な軸心回りに回転させる回転駆動源(図示せず)等を備えている。切削装置100は、X軸移動手段と、Y軸移動手段と、Z軸移動手段及び回転駆動源により、チャックテーブル110と切削手段120とをX軸方向、Y軸方向、Z軸方向及びZ軸と平行な軸心回りに相対的に移動させて、被加工物Wを切削してチップに分割するものである。   The pure water purification apparatus 1 according to the embodiment is disposed adjacent to a cutting apparatus 100 as a processing apparatus shown in FIG. As shown in FIG. 1, the cutting apparatus 100 includes a chuck table 110 that holds a workpiece W, a cutting blade 121 for cutting the workpiece W held on the chuck table 110, and cutting water on the cutting blade 121. A cutting means 120 having a cutting supply nozzle 122 for supplying the X-axis, an X-axis moving means (not shown) for moving the chuck table 110 in the X-axis direction, and a Y-axis movement for moving the cutting means 120 in the Y-axis direction. Means (not shown), Z-axis moving means (not shown) for moving the cutting means 120 in the Z-axis direction, and a rotation drive source (not shown) for rotating the chuck table 110 about an axis parallel to the Z-axis. Etc.). The cutting apparatus 100 includes an X-axis moving unit, a Y-axis moving unit, a Z-axis moving unit, and a rotational drive source to move the chuck table 110 and the cutting unit 120 in the X-axis direction, the Y-axis direction, the Z-axis direction, and the Z-axis. The workpiece W is cut and divided into chips by relatively moving around an axis parallel to the workpiece.

なお、被加工物Wは、本実施形態では、シリコン、サファイア、ガリウムなどを母材とする円板状の半導体ウエーハや光デバイスウエーハである。また、本発明では、被加工物Wは、電子部品に使用される各種セラミック基板、樹脂基板、ガラス基板などであってもよい。被加工物Wは、図1に示すように、粘着シートSに貼着され、粘着シートSに環状フレームFが貼着されて、粘着シートSを介して環状フレームFに装着される。   In the present embodiment, the workpiece W is a disk-shaped semiconductor wafer or optical device wafer whose base material is silicon, sapphire, gallium, or the like. In the present invention, the workpiece W may be various ceramic substrates, resin substrates, glass substrates and the like used for electronic components. As shown in FIG. 1, the workpiece W is attached to the adhesive sheet S, the annular frame F is attached to the adhesive sheet S, and the workpiece W is attached to the annular frame F via the adhesive sheet S.

また、切削装置100は、切削前後の被加工物Wを複数収容するカセットエレベータ130と、カセットエレベータ130に被加工物Wを出し入れする搬出入手段140と、切削後の被加工物Wを洗浄する洗浄手段150と、搬出入手段140とチャックテーブル110と洗浄手段150とに亘って被加工物Wを搬送する搬送手段160と、を備えている。   Further, the cutting apparatus 100 cleans the workpiece W after cutting, a cassette elevator 130 that houses a plurality of workpieces W before and after cutting, a loading / unloading means 140 that puts and removes the workpiece W into and from the cassette elevator 130. A cleaning unit 150, a carry-in / out unit 140, a chuck table 110, and a transport unit 160 that transports the workpiece W across the cleaning unit 150 are provided.

切削装置100は、搬出入手段140によりカセットエレベータ130内から切削前の被加工物Wを取り出し、取り出された被加工物Wを搬送手段160によりチャックテーブル110に搬送する。そして、切削装置100は、チャックテーブル110により被加工物Wを保持し、X軸移動手段と、Y軸移動手段と、Z軸移動手段及び回転駆動源により、チャックテーブル110と切削手段120とをX軸方向、Y軸方向、Z軸方向及びZ軸回りに相対的に移動させて、切削水を供給しながら被加工物Wを切削してチップに分割する。切削装置100は、切削後の被加工物Wを搬送手段160によりチャックテーブル110から洗浄手段150に搬送した後、洗浄手段150により洗浄する。そして、切削装置100は、洗浄後の被加工物Wを搬送手段160により搬出入手段140に搬送し、搬出入手段140によりカセットエレベータ130内に収容する。   The cutting apparatus 100 takes out the workpiece W before cutting from the cassette elevator 130 by the carry-in / out means 140, and conveys the removed workpiece W to the chuck table 110 by the conveying means 160. The cutting apparatus 100 holds the workpiece W by the chuck table 110, and the chuck table 110 and the cutting means 120 are moved by the X-axis moving unit, the Y-axis moving unit, the Z-axis moving unit, and the rotational drive source. The workpiece W is moved relative to the X-axis direction, the Y-axis direction, the Z-axis direction, and the Z-axis direction, and the workpiece W is cut and divided into chips while supplying cutting water. The cutting apparatus 100 transports the workpiece W after cutting from the chuck table 110 to the cleaning unit 150 by the transport unit 160 and then cleans it by the cleaning unit 150. Then, the cutting apparatus 100 conveys the workpiece W after cleaning to the carry-in / out means 140 by the conveyance means 160 and accommodates it in the cassette elevator 130 by the carry-in / out means 140.

純水精製装置1は、切削装置100からの切削屑と切削水などからなる廃液を純水に精製して再利用するためのものである。純水精製装置1は、図2に示すように、廃液収容手段20と、廃液ろ過手段30と、清水収容手段40と、純水精製手段50と、純水温度調整手段90と、図示しない制御手段と、を備える。   The pure water purifying apparatus 1 is for purifying and reusing a waste liquid composed of cutting waste and cutting water from the cutting apparatus 100 into pure water. As shown in FIG. 2, the pure water purification apparatus 1 includes a waste liquid storage means 20, a waste liquid filtration means 30, a fresh water storage means 40, a pure water purification means 50, a pure water temperature adjustment means 90, and a control (not shown). Means.

廃液収容手段20は、切削装置100により排出された廃液を収容するものである。廃液収容手段20は、配管23を通して切削装置100から供給された廃液を収容する廃液タンク21と、廃液タンク21内の廃液を送給する廃液送給ポンプ22を備えている。   The waste liquid storage means 20 stores the waste liquid discharged by the cutting device 100. The waste liquid storage means 20 includes a waste liquid tank 21 that stores the waste liquid supplied from the cutting device 100 through the pipe 23, and a waste liquid supply pump 22 that supplies the waste liquid in the waste liquid tank 21.

廃液ろ過手段30は、廃液収容手段20から送給された廃液から切削屑を除去して清水に精製するものである。廃液ろ過手段30は、廃液収容手段20から送給された廃液が配管31を介して導入される第1のフィルタ32と、廃液が配管31を介して導入される第2のフィルタ33と、第1のフィルタ32及び第2のフィルタ33を着脱自在に設けた清水受けパン36などを備えている。廃液送給ポンプ22と第1のフィルタ32及び第2のフィルタ33とを接続する配管31には、電磁開閉弁34a,34bが設けられている。電磁開閉弁34a,34bが開くと、第1のフィルタ32及び第2のフィルタ33に廃液が導入される。また、配管31には、廃液の圧力を検出する圧力検出手段35が取り付けられている。   The waste liquid filtration means 30 removes cutting waste from the waste liquid fed from the waste liquid storage means 20 and purifies it into fresh water. The waste liquid filtering means 30 includes a first filter 32 into which the waste liquid fed from the waste liquid storage means 20 is introduced through the pipe 31, a second filter 33 into which the waste liquid is introduced through the pipe 31, and a second filter 33. A fresh water receiving pan 36 in which the first filter 32 and the second filter 33 are detachably provided is provided. The piping 31 that connects the waste liquid feed pump 22 to the first filter 32 and the second filter 33 is provided with electromagnetic on-off valves 34a and 34b. When the electromagnetic on-off valves 34 a and 34 b are opened, the waste liquid is introduced into the first filter 32 and the second filter 33. Further, a pressure detection means 35 for detecting the pressure of the waste liquid is attached to the pipe 31.

第1のフィルタ32及び第2のフィルタ33は、導入された廃液をろ過し、廃液中の切削屑を捕捉して、清水に精製する。第1のフィルタ32及び第2のフィルタ33は、精製した清水を清水受けパン36上に流出する。清水受けパン36は、フレキシブルホースなどからなる配管37を通して清水を清水収容手段40に送る。   The first filter 32 and the second filter 33 filter the introduced waste liquid, capture the cutting waste in the waste liquid, and purify it into fresh water. The first filter 32 and the second filter 33 flow the purified fresh water onto the fresh water receiving pan 36. The fresh water receiving pan 36 sends fresh water to the fresh water storage means 40 through a pipe 37 made of a flexible hose or the like.

清水収容手段40は、廃液ろ過手段30からの清水を貯留するものである。清水収容手段40は、配管37を通して廃液ろ過手段30から供給された清水を収容する清水貯留タンク41を備えている。   The fresh water storage means 40 stores fresh water from the waste liquid filtering means 30. The fresh water storage means 40 includes a fresh water storage tank 41 that stores fresh water supplied from the waste liquid filtering means 30 through the pipe 37.

純水精製手段50は、清水を純水に精製するものである。純水精製手段50は、加圧ポンプ51と、紫外線照射手段52と、第1のイオン交換手段53と、第2のイオン交換手段54と、吸引ポンプ55(送出手段に相当)と、精密フィルタ56などを備える。加圧ポンプ51は、清水貯留タンク41内の清水を配管57を通して紫外線照射手段52に送給する。紫外線照射手段52は、導入された清水に紫外線を照射して有機物を分解し殺菌する。紫外線照射手段52は、配管58を通して第1のイオン交換手段53及び第2のイオン交換手段54の流入口71(図3に示す)に接続している。紫外線照射手段52と第1のイオン交換手段53及び第2のイオン交換手段54とを接続する配管58には、電磁開閉弁59a,59bが設けられている。電磁開閉弁59a,59bが開くと、第1のイオン交換手段53及び第2のイオン交換手段54に清水が導入される。   The pure water purifying means 50 purifies fresh water into pure water. The pure water purifying means 50 includes a pressurizing pump 51, an ultraviolet irradiation means 52, a first ion exchange means 53, a second ion exchange means 54, a suction pump 55 (corresponding to a delivery means), a precision filter. 56 and the like. The pressurizing pump 51 supplies the fresh water in the fresh water storage tank 41 to the ultraviolet irradiation means 52 through the pipe 57. The ultraviolet irradiation means 52 irradiates the introduced fresh water with ultraviolet rays to decompose and sterilize organic substances. The ultraviolet irradiation means 52 is connected to the inlet 71 (shown in FIG. 3) of the first ion exchange means 53 and the second ion exchange means 54 through the pipe 58. Electromagnetic on-off valves 59a and 59b are provided in a pipe 58 that connects the ultraviolet irradiation means 52 to the first ion exchange means 53 and the second ion exchange means 54. When the electromagnetic on-off valves 59a and 59b are opened, fresh water is introduced into the first ion exchange means 53 and the second ion exchange means 54.

第1のイオン交換手段53及び第2のイオン交換手段54は、清水収容手段40から送水される清水をイオン交換して純水に精製するものである。また、第1のイオン交換手段53及び第2のイオン交換手段54の流出口72(図3に示す)と吸引ポンプ55と精密フィルタ56とを接続する配管60には、第1のイオン交換手段53及び第2のイオン交換手段54の流出口72からの純水の圧力を検出する圧力検出手段61a,61bが取り付けられている。   The 1st ion exchange means 53 and the 2nd ion exchange means 54 ion-exchange the fresh water sent from the fresh water storage means 40, and refine | purify it to a pure water. Further, the first ion exchange means 53 and the second ion exchange means 54 are connected to the outlet 72 (shown in FIG. 3), the pipe 60 connecting the suction pump 55 and the precision filter 56 with the first ion exchange means. 53 and pressure detection means 61a and 61b for detecting the pressure of pure water from the outlet 72 of the second ion exchange means 54 are attached.

吸引ポンプ55は、圧力検出手段61a,61bよりも下流側に配置され、配管60内の第1のイオン交換手段53及び第2のイオン交換手段54によって精製された純水を第1のイオン交換手段53及び第2のイオン交換手段54から所定の水圧で精密フィルタ56及び純水温度調整手段90に向けて送出する。なお、本実施形態では、吸引ポンプ55は、第1のイオン交換手段53及び第2のイオン交換手段54によって精製された純水を所定の圧力としての0.3MPa(ゲージ圧)で配管60を通して精密フィルタ56に送出する。精密フィルタ56は、イオン交換樹脂74(図3に示す)などの樹脂屑などの微細な物質を捕捉するものである。純水温度調整手段90は、純水を所定温度に調整して切削装置100の切削水供給手段に循環するものである。   The suction pump 55 is disposed downstream of the pressure detection means 61a and 61b, and the pure water purified by the first ion exchange means 53 and the second ion exchange means 54 in the pipe 60 is subjected to the first ion exchange. It is sent from the means 53 and the second ion exchange means 54 toward the precision filter 56 and the pure water temperature adjusting means 90 at a predetermined water pressure. In this embodiment, the suction pump 55 passes the pure water purified by the first ion exchange means 53 and the second ion exchange means 54 through the pipe 60 at a predetermined pressure of 0.3 MPa (gauge pressure). Send to precision filter 56. The precision filter 56 captures fine substances such as resin waste such as ion exchange resin 74 (shown in FIG. 3). The pure water temperature adjusting means 90 adjusts the pure water to a predetermined temperature and circulates it to the cutting water supply means of the cutting apparatus 100.

第1のイオン交換手段53及び第2のイオン交換手段54は、図3に示すように、流入口71と流出口72を備え、流出口72に配管60を介して吸引ポンプ55が連結される容器73と、容器73に収容されるイオン交換樹脂74とから構成される。   As shown in FIG. 3, the first ion exchange means 53 and the second ion exchange means 54 include an inflow port 71 and an outflow port 72, and the suction pump 55 is connected to the outflow port 72 via a pipe 60. It is comprised from the container 73 and the ion exchange resin 74 accommodated in the container 73. FIG.

容器73は、イオン交換樹脂74を収容するものである。容器73は、図3に示すように、流入口71を備える天井部73aと、流出口72を備えかつ天井部73aに対面しかつ天井部73aよりも下方に配置される底部73bと、天井部73aと底部73bとを連結する円筒状の側部73cとを有して、流入口71と流出口72とを除いて内部が密閉されている。流入口71と流出口72とは、円筒状に形成され、天井部73a、底部73b及び側部73cと同軸に配置されている。天井部73aと底部73bとは、外観が円錐台形状に形成されている。天井部73aの表面の容器73全体の軸心P(図3に一点鎖線で示す)とのなす角度Θ1は、底部73bの表面の軸心Pとのなす角度Θ2よりも大きい。   The container 73 accommodates the ion exchange resin 74. As shown in FIG. 3, the container 73 includes a ceiling portion 73a having an inflow port 71, a bottom portion 73b having an outflow port 72, facing the ceiling portion 73a, and disposed below the ceiling portion 73a, and a ceiling portion. It has a cylindrical side portion 73c that connects 73a and the bottom portion 73b, and the inside is sealed except for the inflow port 71 and the outflow port 72. The inflow port 71 and the outflow port 72 are formed in a cylindrical shape, and are arranged coaxially with the ceiling part 73a, the bottom part 73b, and the side part 73c. The ceiling part 73a and the bottom part 73b are formed in a truncated cone shape. An angle Θ1 formed with the axis P of the entire container 73 on the surface of the ceiling 73a (indicated by a dashed line in FIG. 3) is larger than an angle Θ2 formed with the axis P of the surface of the bottom 73b.

容器73は、PO(polyolefin)、PET(polyethylene terephthalate)、PE(polyethylene)、PVC(polyvinyl chloride)などで構成され、単層樹脂で形成されている。容器73は、0〜−0.01MPa(ゲージ圧)程度の内部の水圧に耐えることができる程度の強度を有している。このために、容器73は、内部の水圧が大きく変化すると、内部の水圧に応じて変形することとなる。容器73は、射出成型、ブロー成型、押し出し成型などの安価に大量に生産可能な方法により製造される。   The container 73 is made of PO (polyolefin), PET (polyethylene terephthalate), PE (polyethylene), PVC (polyvinyl chloride), or the like, and is formed of a single layer resin. The container 73 has a strength that can withstand an internal water pressure of about 0 to -0.01 MPa (gauge pressure). For this reason, if the internal water pressure changes greatly, the container 73 will be deformed according to the internal water pressure. The container 73 is manufactured by a method that can be mass-produced at low cost, such as injection molding, blow molding, and extrusion molding.

また、容器73は、清水を供給する配管58を流入口71に接続する接続手段75と、純水を送出する配管60を流出口72に接続する流出側接続手段76とを備えて、常に上方の流入口71から清水が容器73内に供給される。なお、接続手段75と流出側接続手段76とは、構成が等しいので、以下、接続手段75を代表して説明する。   The container 73 includes a connecting means 75 for connecting a pipe 58 for supplying fresh water to the inflow port 71 and an outflow side connecting means 76 for connecting the pipe 60 for sending pure water to the outflow port 72. Fresh water is supplied into the container 73 from the inflow port 71. Since the connecting means 75 and the outflow side connecting means 76 have the same configuration, the connecting means 75 will be described below as a representative.

接続手段75は、配管58を流入口71に接続する接続部材77と、配管58と接続部材77に固定可能で、接続部材77を流入口71に固定可能な着脱キャップ78とを備えている。接続部材77は、図4(a)及び図4(b)に示すように、配管58と連結し、配管58を流入口71に固定する連結固定部77aと、容器73内に挿入され、清水を容器73に供給する導入管部77bを一体に備える。連結固定部77aは、円筒状に形成され、かつ、流入口71内に通されて容器73外に突出するとともに、配管58内に挿入されて配管58と連結する。   The connection means 75 includes a connection member 77 that connects the pipe 58 to the inflow port 71, and a detachable cap 78 that can be fixed to the pipe 58 and the connection member 77 and can fix the connection member 77 to the inflow port 71. As shown in FIGS. 4A and 4B, the connecting member 77 is connected to the pipe 58, and is inserted into the container 73 and a connecting and fixing portion 77a that fixes the pipe 58 to the inlet 71. Is integrally provided with an introduction pipe portion 77 b for supplying the liquid to the container 73. The connection fixing portion 77 a is formed in a cylindrical shape, passes through the inflow port 71 and protrudes out of the container 73, and is inserted into the pipe 58 to be connected to the pipe 58.

導入管部77bは、連結固定部77aの容器73の内側の端部に連なっている。導入管部77bは、外観が円錐台形状に形成されている。導入管部77bの流出口72と対面する底部77cは、連結固定部77aの外径よりも広く形成されている。導入管部77bの連結固定部77aと底部77cとを連結する側面77dは、連結固定部77aから底部77cに向かうにしたがって徐々に外径が広くなる様に軸心Pに対して傾斜している。この傾斜した側面77dには、清水を容器73内に導く噴出口77eが周方向沿って間隔をあけて形成されている。本実施形態では、噴出口77eは、連結固定部77aから底部77cに向かう方向に直線状に延びている。なお、底部77cには、開口や孔などが一切設けられていない。   The introduction pipe part 77b is connected to the inner end of the container 73 of the connection fixing part 77a. The introduction pipe portion 77b is formed in a truncated cone shape. The bottom 77c facing the outflow port 72 of the introduction pipe 77b is formed wider than the outer diameter of the connecting and fixing 77a. A side surface 77d that connects the connecting and fixing portion 77a and the bottom portion 77c of the introduction pipe portion 77b is inclined with respect to the axis P so that the outer diameter gradually increases from the connecting and fixing portion 77a toward the bottom portion 77c. . On the inclined side surface 77d, jet outlets 77e for guiding fresh water into the container 73 are formed at intervals along the circumferential direction. In the present embodiment, the jet outlet 77e extends linearly in a direction from the connection fixing portion 77a toward the bottom portion 77c. The bottom 77c is not provided with any openings or holes.

導入管部77bは、配管58を通して清水が供給される。導入管部77bに供給された清水は、底部77cが邪魔板となり、噴出口77eを通して容器73内に供給される。そして、導入管部77bの噴出口77eから容器73内に供給される清水は、底部77cによって跳ね返されて、噴出口77eから斜め上方に向かって放射状に噴出する。   The introduction pipe portion 77 b is supplied with fresh water through the pipe 58. The fresh water supplied to the introduction pipe portion 77b serves as a baffle at the bottom 77c, and is supplied into the container 73 through the spout 77e. And the fresh water supplied in the container 73 from the jet outlet 77e of the introduction pipe part 77b is bounced off by the bottom part 77c, and is ejected radially diagonally upward from the jet outlet 77e.

また、流出側接続手段76の接続部材77は、図3に示すように、連結固定部77aが流出口72内に通されて容器73外に突出するとともに、配管60内に挿入されて配管60と連結し、導入管部77bが、底部77cが流入口71と対面した状態で容器73内に挿入され、側面77dが連結固定部77aから底部77cに向かうにしたがって徐々に外径が広くなる様に軸心Pに対して傾斜している。流出側接続手段76の接続部材77は、イオン交換樹脂74により精製された純水を噴出口77eから取り込んで、取り込んだ純水を導入管部77bを通して配管60に供給する。   Further, as shown in FIG. 3, the connection member 77 of the outflow side connection means 76 is inserted into the pipe 60 and inserted into the pipe 60 while the coupling fixing portion 77 a is passed through the outlet 72 and protrudes out of the container 73. The introduction pipe portion 77b is inserted into the container 73 with the bottom portion 77c facing the inflow port 71, and the outer diameter gradually increases as the side surface 77d moves from the connection fixing portion 77a toward the bottom portion 77c. Is inclined with respect to the axis P. The connection member 77 of the outflow side connection means 76 takes in pure water purified by the ion exchange resin 74 from the jet outlet 77e, and supplies the taken pure water to the pipe 60 through the introduction pipe portion 77b.

着脱キャップ78は、接続部材77の連結固定部77aを流入口71及び流出口72に着脱自在とするものである。着脱キャップ78は、二層構造であったり、複数の材料を組み合わせて構成されてもよい。イオン交換樹脂74としては、アニオン交換樹脂、カチオン交換樹脂のうちの少なくとも一方などが用いられる。なお、本実施形態では、イオン交換樹脂74としては、アニオン交換樹脂、カチオン交換樹脂の両方が所定の割合で容器73内に充填されている。カチオン樹脂は、アニオン樹脂よりも比重が大きい。イオン交換樹脂74は、清水が供給されると、イオン分が吸着して、体積収縮を起こし、イオン交換樹脂74間に隙間を生じさせる。   The detachable cap 78 allows the connecting and fixing portion 77 a of the connecting member 77 to be freely attached to and detached from the inflow port 71 and the outflow port 72. The detachable cap 78 may have a two-layer structure or a combination of a plurality of materials. As the ion exchange resin 74, at least one of an anion exchange resin and a cation exchange resin is used. In the present embodiment, as the ion exchange resin 74, both the anion exchange resin and the cation exchange resin are filled in the container 73 at a predetermined ratio. Cationic resins have a higher specific gravity than anionic resins. When fresh water is supplied to the ion exchange resin 74, ions are adsorbed to cause volume contraction and create a gap between the ion exchange resins 74.

第1のイオン交換手段53及び第2のイオン交換手段54は、流入口71から導入された清水を容器73内のイオン交換樹脂74間に導き、イオン交換樹脂74によりイオン交換して純水に精製し、流出口72から吸引ポンプ55に送り出す。   The first ion exchange means 53 and the second ion exchange means 54 guide the fresh water introduced from the inflow port 71 between the ion exchange resins 74 in the container 73, and exchange ions with the ion exchange resin 74 to obtain pure water. Purified and sent out from the outlet 72 to the suction pump 55.

制御手段は、純水精製装置1を構成する上述した構成要素をそれぞれ制御して、純水精製装置1により廃液を純水に精製させるものである。制御手段は、圧力検出手段35,61a,61bの検出結果に基いて、電磁開閉弁34a,34b,59a,59b、加圧ポンプ51及び吸引ポンプ55を制御して、廃液を廃液収容手段20に収容した後、廃液ろ過手段30でろ過して清水に精製し、清水を清水収容手段40に収容した後、純水精製手段50で純水に精製し、精密フィルタ56及び純水温度調整手段90に向けて送出して、純水精製装置1により廃液を純水に精製させる。なお、制御手段は、例えばCPU等で構成された演算処理装置やROM、RAM等を備える図示しないマイクロプロセッサを主体として構成されている。また、制御手段には、純水精製開始情報などの処理情報を入力する操作盤(図示せず)が接続されている。   The control means controls the above-described components constituting the pure water purifying apparatus 1 so that the waste water is purified to pure water by the pure water purifying apparatus 1. The control means controls the electromagnetic on-off valves 34a, 34b, 59a, 59b, the pressurization pump 51, and the suction pump 55 based on the detection results of the pressure detection means 35, 61a, 61b, and supplies the waste liquid to the waste liquid storage means 20. After being accommodated, it is filtered by the waste liquid filtering means 30 to be purified into fresh water, and after the fresh water is accommodated in the fresh water accommodating means 40, it is purified to pure water by the pure water purifying means 50, and the precision filter 56 and the pure water temperature adjusting means 90 The waste liquid is purified to pure water by the pure water purifier 1. Note that the control means is configured mainly by a microprocessor (not shown) provided with an arithmetic processing unit constituted by a CPU or the like, a ROM, a RAM, or the like. Further, an operation panel (not shown) for inputting processing information such as pure water purification start information is connected to the control means.

制御手段は、純水精製装置1に廃液を純水に精製させる際には、吸引ポンプ55から精密フィルタ56に送出される純水の圧力を0.3MPa(ゲージ圧)に調整する。そして、制御手段は、圧力検出手段61a,61bの検出結果に基いて、配管60内即ち流出口72から流出される純水の圧力が0MPa(ゲージ圧)から−0.01MPa(ゲージ圧)となるように、加圧ポンプ51を制御する。即ち、制御手段は、第1のイオン交換手段53及び第2のイオン交換手段54の容器73内の純水の圧力を0MPa(ゲージ圧)から−0.01MPa(ゲージ圧)に維持する。   The control means adjusts the pressure of pure water sent from the suction pump 55 to the precision filter 56 to 0.3 MPa (gauge pressure) when the pure water purifier 1 purifies the waste liquid into pure water. Based on the detection results of the pressure detection means 61a and 61b, the control means sets the pressure of pure water flowing out from the pipe 60, that is, the outlet 72, from 0 MPa (gauge pressure) to -0.01 MPa (gauge pressure). Thus, the pressurizing pump 51 is controlled. That is, the control means maintains the pressure of pure water in the containers 73 of the first ion exchange means 53 and the second ion exchange means 54 from 0 MPa (gauge pressure) to -0.01 MPa (gauge pressure).

なお、第1のイオン交換手段53及び第2のイオン交換手段54の容器73内の純水の圧力が−0.01MPa(ゲージ圧)よりも低くなると、容器73内にイオン交換樹脂74に付着していた気泡が大量に発生して、イオン交換樹脂74の性能を充分に発揮できなくなる。また、第1のイオン交換手段53及び第2のイオン交換手段54の容器73内の純水の圧力が0MPa(ゲージ圧)よりも高くなると、容器73内に正圧がかかり、容器73を頑丈な圧力容器とする必要があるからである。こうすることで、純水精製装置1は、吸引ポンプ55によって第1のイオン交換手段53及び第2のイオン交換手段54にかかる吸引力を、加圧ポンプ51の清水の加圧によって緩和する。   When the pressure of pure water in the container 73 of the first ion exchange means 53 and the second ion exchange means 54 becomes lower than −0.01 MPa (gauge pressure), the ion exchange resin 74 adheres to the container 73. A large amount of the generated bubbles are generated, and the performance of the ion exchange resin 74 cannot be sufficiently exhibited. Further, when the pressure of pure water in the container 73 of the first ion exchange means 53 and the second ion exchange means 54 becomes higher than 0 MPa (gauge pressure), a positive pressure is applied in the container 73, and the container 73 is made strong. This is because it is necessary to use a pressure vessel. By doing so, the pure water purifier 1 relaxes the suction force applied to the first ion exchange means 53 and the second ion exchange means 54 by the suction pump 55 by pressurizing the fresh water of the pressurization pump 51.

以上のように、実施形態に係る純水精製装置1によれば、流入口71を容器73の上方に設け、流出口72を容器73の下方に設けて、イオン交換手段53,54の容器73内において常に上方から下方に向けて清水を流す、所謂ダウンフローで清水を通水する構成としている。このために、純水精製装置1は、イオン交換手段53,54への清水の供給が停止されても、イオン吸着などにより体積が変化したイオン交換樹脂74同士が容器73内で移動することを抑制することができる。したがって、純水精製装置1は、イオン交換手段53,54への清水の供給が停止されても、容器73内でイオン交換樹脂74であるアニオン樹脂とカチオン樹脂が分離する事を抑制することができる。よって、純水精製装置1は、清水の供給、停止が繰り返されても、イオン交換樹脂74の分離を抑制でき、イオン交換の効果を充分に発揮することができる、という効果を奏する。   As described above, according to the pure water purifying apparatus 1 according to the embodiment, the inlet 71 is provided above the container 73, the outlet 72 is provided below the container 73, and the containers 73 of the ion exchange means 53 and 54 are provided. In the inside, it is set as the structure which flows clear water by what is called a down flow to which clear water is always flowed from upper direction toward the downward direction. For this reason, the pure water purifying apparatus 1 indicates that even if the supply of fresh water to the ion exchange means 53, 54 is stopped, the ion exchange resins 74 whose volumes have changed due to ion adsorption or the like move within the container 73. Can be suppressed. Therefore, even if the supply of fresh water to the ion exchange means 53 and 54 is stopped, the pure water purifier 1 can prevent the anion resin and the cation resin that are the ion exchange resin 74 from being separated in the container 73. it can. Therefore, even if supply and stop of fresh water are repeated, the pure water purification apparatus 1 can suppress the separation of the ion exchange resin 74, and has an effect that the effect of ion exchange can be sufficiently exhibited.

また、純水精製装置1は、イオン交換手段53,54の接続部材77が底部77cと、噴出口77eが設けられた側面77dとを有して外観が円錐台形状に形成されている。このために、純水精製装置1は、イオン交換手段53,54の接続部材77内に導かれた清水が底部77cに衝突して、導入管部77bの傾斜した側面77dに設けられた噴出口77eから清水が斜め上方に放射状に噴出して容器73内に供給される。したがって、純水精製装置1は、使用開始時の初期の通水水張り時でも、イオン交換手段53,54の容器73内から効率的に空気を排出でき、且つ、ダウンフローの最短経路で清水が排出されることが無く、容器73内の隅々のイオン交換樹脂74に清水を行き渡らせることができる。よって、純水精製装置1は、できる限りイオン交換樹脂74に長く清水を接触させることができ、清水のイオン交換、即ち純水への精製を確実に実施できるという効果も奏する。   Further, the pure water purifying apparatus 1 has a connecting member 77 of the ion exchange means 53, 54 having a bottom 77c and a side surface 77d provided with a jet outlet 77e, and the appearance is formed in a truncated cone shape. For this purpose, the pure water purifying apparatus 1 has a jet outlet provided on the inclined side surface 77d of the introduction pipe portion 77b when the clear water introduced into the connection member 77 of the ion exchange means 53, 54 collides with the bottom portion 77c. From 77e, fresh water is ejected radially upward and supplied into the container 73. Therefore, the pure water purifying apparatus 1 can efficiently exhaust air from the inside of the container 73 of the ion exchange means 53 and 54 even when the initial water flow is filled at the start of use, and fresh water can be discharged through the shortest path of downflow. Without being discharged, fresh water can be spread over the ion exchange resin 74 in every corner of the container 73. Therefore, the pure water purification apparatus 1 can bring fresh water into contact with the ion exchange resin 74 for as long as possible, and also has an effect that ion exchange of fresh water, that is, purification into pure water can be performed with certainty.

さらに、純水精製装置1は、イオン交換手段53,54の容器73の天井部73aの表面の軸心Pに対する角度Θ1が、底部73bの表面の軸心Pに対する角度Θ2よりも大きいので、イオン交換手段53,54の容器73の上下を間違うことを抑制することができる。特に、純水精製装置1は、イオン交換手段53,54の容器73内に複数のイオン交換樹脂74を多層化させて収容した場合に、上下の設置即ち通水方向を誤ることを抑制することができる。   Further, in the pure water purifying apparatus 1, since the angle Θ1 with respect to the axis P of the surface of the ceiling 73a of the vessel 73 of the ion exchange means 53, 54 is larger than the angle Θ2 with respect to the axis P of the surface of the bottom 73b, It can suppress that the container 73 of the exchange means 53 and 54 is upside down. In particular, the pure water purifying apparatus 1 suppresses erroneous installation of the upper and lower sides, that is, the water flow direction when a plurality of ion exchange resins 74 are accommodated in the containers 73 of the ion exchange means 53 and 54 in a multilayered manner. Can do.

さらに、純水精製装置1は、イオン交換手段53,54の容器73の天井部73aの表面の軸心Pに対する角度Θ1が、底部73bの表面の軸心Pに対する角度Θ2よりも大きいので、流入口71から導入され噴出口77eから斜め上方に噴出される清水が、天井部73aに干渉することを抑制できる。したがって、純水精製装置1は、流入口71から導入され噴出口77eから噴出される清水を容器73内の隅々のイオン交換樹脂74に行き渡らせることができる。   Further, in the pure water purifying apparatus 1, the angle Θ1 with respect to the axis P of the surface of the ceiling 73a of the vessel 73 of the ion exchange means 53, 54 is larger than the angle Θ2 with respect to the axis P of the surface of the bottom 73b. It can suppress that the clear water introduce | transduced from the inlet_port | entrance 71 and ejected diagonally upward from the jet outlet 77e interferes with the ceiling part 73a. Therefore, the pure water purifier 1 can spread the fresh water introduced from the inlet 71 and ejected from the outlet 77e to the ion exchange resins 74 in every corner of the container 73.

また、純水精製装置1は、イオン交換手段53,54の容器73の天井部73aの表面の軸心Pに対する角度Θ1が、底部73bの表面の軸心Pに対する角度Θ2よりも大きいので、容器73の下端部ではイオン交換されて精製された純水を流出口72に速やかに集めることができる。   Further, the pure water purifying apparatus 1 has an angle Θ1 with respect to the axis P of the surface of the ceiling 73a of the container 73 of the ion exchange means 53, 54 larger than the angle Θ2 with respect to the axis P of the surface of the bottom 73b. At the lower end of 73, pure water purified by ion exchange can be quickly collected at the outlet 72.

第1のイオン交換手段53及び第2のイオン交換手段54の容器73にかかる水圧が低くてすむため、例えばPO(polyolefin)やPET(polyethylene terephthalate)などの樹脂により単層で構成された容器73をイオン交換手段53,54の容器に用いることができる。このために、使用済みのイオン交換樹脂74を容器73ごと廃棄する際に、イオン交換手段53,54が軽量のため処理作業も容易になり、処理費用も安くすむという効果もある。また、イオン交換手段53,54が軽量で単純な構成であるため、輸送に係るコストも安く、イオン交換樹脂74の交換も容易となる。したがって、純水精製装置1は、ランニングコストの低コスト化を図ることができる。   Since the water pressure applied to the containers 73 of the first ion exchange means 53 and the second ion exchange means 54 can be low, the container 73 is composed of a single layer of a resin such as PO (polyolefin) or PET (polyethylene terephthalate). Can be used as a container for the ion exchange means 53 and 54. For this reason, when the used ion exchange resin 74 is discarded together with the container 73, the ion exchange means 53 and 54 are lightweight, so that the processing work is facilitated and the processing cost can be reduced. In addition, since the ion exchange means 53 and 54 are light and simple, the transportation cost is low and the exchange of the ion exchange resin 74 is easy. Therefore, the pure water purifier 1 can reduce the running cost.

さらに、純水精製装置1は、イオン交換手段53,54の容器73を水圧に応じて変形しやすい安価な構成にするためにも、イオン交換手段53,54の容器73内において常に上方から下方に向けて清水を流すので、イオン交換樹脂74の分離を抑制でき、イオン交換の効果を充分に発揮することができる、という効果を奏する。   Further, the pure water purifying apparatus 1 always has a configuration in which the container 73 of the ion exchange means 53, 54 is easily deformed in accordance with the water pressure and is always downward from above in the container 73 of the ion exchange means 53, 54. Since fresh water is poured toward the surface, the separation of the ion exchange resin 74 can be suppressed, and the effect of ion exchange can be sufficiently exhibited.

〔変形例〕
本発明の実施形態の変形例に係る純水精製装置を図面に基いて説明する。図5(a)は、実施形態の変形例に係る純水精製装置のイオン交換手段の接続部材を示す側部図である。図5(b)は、実施形態の変形例に係る純水精製装置のイオン交換手段の接続部材を示す上面図である。なお、図5において、実施形態と同一部分には、同一符号を付して説明を省略する。
[Modification]
The pure water refiner | purifier which concerns on the modification of embodiment of this invention is demonstrated based on drawing. Fig.5 (a) is a side view which shows the connection member of the ion exchange means of the pure water refiner | purifier which concerns on the modification of embodiment. FIG.5 (b) is a top view which shows the connection member of the ion exchange means of the pure water refiner | purifier which concerns on the modification of embodiment. In FIG. 5, the same parts as those of the embodiment are denoted by the same reference numerals and description thereof is omitted.

実施形態の変形例に係る純水精製装置1の接続手段75,76の接続部材77は、導入管部77bの側面77dに清水を容器73内に導く噴出口77eが周方向沿って直線状に形成されている。実施形態の変形例では、噴出口77eは、側面77dの略全周に亘って設けられている。なお、本発明では、噴出口77eは、周方向沿って等間隔に複数形成されてもよい。変形例に係る純水精製装置1の接続手段75,76の接続部材77の導入管部77bは、底部77cが供給された清水の邪魔板となり、清水を噴出口77eを通して容器73内に供給する。そして、導入管部77bの噴出口77eから容器73内に供給される清水は、底部77cによって跳ね返されて、噴出口77eから斜め上方に向かって放射状に噴出する。   In the connection member 77 of the connection means 75, 76 of the pure water purifying apparatus 1 according to the modification of the embodiment, the jet outlet 77e that guides fresh water into the container 73 to the side surface 77d of the introduction pipe portion 77b is linear along the circumferential direction. Is formed. In the modification of the embodiment, the ejection port 77e is provided over substantially the entire circumference of the side surface 77d. In the present invention, a plurality of jet outlets 77e may be formed at equal intervals along the circumferential direction. The introduction pipe portion 77b of the connection member 77 of the connection means 75, 76 of the pure water purifying apparatus 1 according to the modification serves as a baffle plate for the fresh water supplied to the bottom portion 77c, and supplies the fresh water into the container 73 through the spout 77e. . And the fresh water supplied in the container 73 from the jet outlet 77e of the introduction pipe part 77b is bounced off by the bottom part 77c, and is ejected radially diagonally upward from the jet outlet 77e.

実施形態の変形例に係る純水精製装置1によれば、実施形態と同様に、イオン交換手段53,54の容器73内において上方から下方に向けて清水を流す、所謂ダウンフローで清水を通水する構成としているために、イオン交換の効果を充分に発揮することができる、という効果を奏する。   According to the pure water purifying apparatus 1 according to the modified example of the embodiment, as in the embodiment, the fresh water is passed through the so-called down flow in which the fresh water is flowed from the upper side to the lower side in the container 73 of the ion exchange means 53 and 54. Since it is set as the structure which waters, there exists an effect that the effect of ion exchange can fully be exhibited.

本発明では、純水精製装置1は、切削装置100に限ることなく、加工装置としての研磨装置や研削装置からの廃液を純水に精製してもよい。   In the present invention, the pure water purifying apparatus 1 is not limited to the cutting apparatus 100 and may purify waste liquid from a polishing apparatus or a grinding apparatus as a processing apparatus into pure water.

なお、本発明は上記実施形態に限定されるものではない。即ち、本発明の骨子を逸脱しない範囲で種々変形して実施することができる。   The present invention is not limited to the above embodiment. That is, various modifications can be made without departing from the scope of the present invention.

1 純水精製装置
53 第1のイオン交換手段
54 第2のイオン交換手段
55 吸引ポンプ(送出手段)
58,60 配管
71 流入口
72 流出口
73 容器
73a 天井部
73b 底部
73c 側部
74 イオン交換樹脂
75 接続手段
77a 連結固定部
77b 導入管部
77c 底部
77d 側面
77e 噴出口
DESCRIPTION OF SYMBOLS 1 Pure water refinement | purification apparatus 53 1st ion exchange means 54 2nd ion exchange means 55 Suction pump (delivery means)
58, 60 Piping 71 Inlet 72 Outlet 73 Container 73a Ceiling part 73b Bottom part 73c Side part 74 Ion exchange resin 75 Connection means 77a Connection fixing part 77b Introducing pipe part 77c Bottom part 77d Side face 77e Spout

Claims (1)

送水される清水を純水に精製するイオン交換手段と、該イオン交換手段によって精製された純水を該イオン交換手段から送出する送出手段と、を備える純水精製装置であって、
該イオン交換手段は、
イオン交換樹脂と
流入口を備える天井部と、送出口を備える底部と、該天井部と該底部とを連結する側部とを有し、該イオン交換樹脂を収容する容器と、から構成され、
上方の流入口から該清水が該容器に供給され
該容器は、該清水を供給する配管を該流入口に接続する接続手段を備え、
該接続手段は、
該配管と連結し、該配管を該流入口に固定する連結固定部と、
該容器に挿入され、該清水を該容器に供給する導入管部を備え、
該導入管部は、
底部が広い円錐台形状で、傾斜した側部に噴出口が周方向沿って形成され、
該底部が邪魔板となり、該導入管部の該噴出口から供給される該清水は、該噴出口から放射状に噴出することを特徴とする純水精製装置。
A pure water purifier comprising: ion exchange means for purifying purified water to be purified into pure water; and sending means for sending pure water purified by the ion exchange means from the ion exchange means,
The ion exchange means
A container having an ion exchange resin and a ceiling portion having an inlet, a bottom portion having a delivery port, a side portion connecting the ceiling portion and the bottom portion, and containing the ion exchange resin;
The fresh water is supplied to the container from the upper inlet ,
The container includes connection means for connecting a pipe for supplying the fresh water to the inflow port,
The connecting means includes
A connecting and fixing part that connects to the pipe and fixes the pipe to the inlet;
An introduction pipe part that is inserted into the container and supplies the fresh water to the container;
The introduction pipe part is
The bottom is a wide frustoconical shape, and a spout is formed along the circumferential direction on the inclined side.
Said bottom is a baffle plate,該清water supplied from該噴outlet of the introduction pipe portion, pure water purifier you characterized in that ejected radially from該噴outlet.
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