JPH079493U - Mashimizu Demineralizer - Google Patents
Mashimizu DemineralizerInfo
- Publication number
- JPH079493U JPH079493U JP4320393U JP4320393U JPH079493U JP H079493 U JPH079493 U JP H079493U JP 4320393 U JP4320393 U JP 4320393U JP 4320393 U JP4320393 U JP 4320393U JP H079493 U JPH079493 U JP H079493U
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- Prior art keywords
- water
- receiving tank
- fresh water
- treated water
- treated
- Prior art date
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Abstract
(57)【要約】
【目的】コンパクトな構造で、水道水を安全でしかも天
然の涌き水のようなうまい水に連続的に改質することが
できる真清水造水装置を提供する。
【構成】揚水循環ポンプ９を配した架台１の上または側
部に処理水受水タンク２を設け、該処理水受水タンク２
内に前記揚水循環ポンプ９に接続される原水取り入れ管
５の上端を開口させるとともに、処理水受水タンク２内
の水位に応じて原水導管６を開閉する制御弁７を設け、
前記揚水循環ポンプ９の吐出配管９０にはオゾン発生器
１２と接続したエゼクタ１１を介して反応器３を接続
し、該反応器３の出口側には積層ろ材４２を充填した造
水器４を接続し、該造水器４の出口側を前記処理水受水
タンク２に接続し、処理水受水タンク２の適所には処理
水取出し部を設けた。
(57) [Summary] [Purpose] To provide a fresh water desalination device which has a compact structure and is capable of continuously reforming tap water into a safe and delicious water such as natural sprinkling water. [Structure] A treated water receiving tank 2 is provided on or on a side of a frame 1 on which a pumped water circulation pump 9 is arranged, and the treated water receiving tank 2 is provided.
A control valve 7 that opens the upper end of the raw water intake pipe 5 connected to the pumped water circulation pump 9 and opens and closes the raw water conduit 6 according to the water level in the treated water receiving tank 2 is provided.
The reactor 3 is connected to the discharge pipe 90 of the pumped water circulation pump 9 through the ejector 11 connected to the ozone generator 12, and the fresh water generator 4 filled with the laminated filter medium 42 is provided on the outlet side of the reactor 3. The treated water receiving tank 2 was connected to the outlet side of the fresh water generator 4, and a treated water take-out section was provided at an appropriate position of the treated water receiving tank 2.
Description
【０００１】[0001]
本考案は真清水造水装置に関する。 The present invention relates to a fresh water freshener.
【０００２】[0002]
水は生活や料理等に欠くことのできない重要なものであるが、近年水源地とし ての河川の汚濁化に伴い水道原水の水質は極めて悪化しており、このため水道水 は殺菌のための塩素等が多量に含まれ、またトリハロメタンなどの有害物質が含 まれ、さらに塩素投入によって酸性化し、赤水や藻類などによって濁度も不良化 している。 こうした水道水の水質を改善する手段として従来種々のものが提案されている が、そのほとんどはフィルターや活性炭などを充填したものにすぎず、それを蛇 口に取付け蛇口を開くと活性炭などと接触させて流下させるいわゆる瞬時通水式 の簡易浄水器であった。このため、塩素の除去や濁度の改善にはある程度の効果 はあるものの、使用によってフィルターが汚れるためかえって水質が悪化し、い わんやミネラル成分を含んだおいしい水を得ることはできないという問題があっ た。 ことに飲食店などにおいては、水道水を調理用、飲料用として大量に使用し、 また冷水機能付きのタンクに水道水を導いてセルフサービス式に飲用に供してい るが、この場合のタンクは浄水機能がないため、不衛生でまずい水しか飲めない という問題があった。 Water is an important water indispensable for daily life and cooking, but in recent years, the quality of tap water has deteriorated significantly due to the pollution of rivers, which are the source of water. It contains a large amount of chlorine and other harmful substances such as trihalomethane, is acidified by chlorine addition, and has a poor turbidity due to red water and algae. Various methods have been proposed so far to improve the quality of tap water, but most of them are only those filled with a filter or activated carbon, and when they are attached to the faucet, the faucet comes into contact with the activated carbon. It was a simple water purifier of the so-called instantaneous water flow type that allowed it to flow down. For this reason, although there is some effect in removing chlorine and improving turbidity, there is a problem in that the quality of the water deteriorates because the filter becomes dirty due to its use, and it is not possible to obtain delicious water that contains, for example, minerals. there were. Especially in restaurants, tap water is used in large quantities for cooking and drinking, and tap water is led to a tank with a chilled water function for self-service drinking. Since there is no water purification function, there was a problem that only poor water could be consumed due to unsanitary conditions.
【０００３】 本考案は前記のような問題点を解消するために考案されたもので、その目的と するところは、コンパクトな構造で、水道水を安全でしかも天然の涌き水のよう なうまい水に連続的に改質することができる真清水造水装置を提供することにあ る。 本考案による真清水造水装置は、飲食店、ホテル、一般家庭の厨房等に配置し て調理用、飲料用あるいは製氷用の水を作ったり、あるいはまたオフィスビルや 飲食店などの適所に設置してセルフサービス飲料用の水を作るなどの用途に好適 であり、冷凍機と組み合わせて冷水とすることもできる。The present invention was devised to solve the above-mentioned problems, and its purpose is to make tap water into a safe and delicious water like natural sprinkling water. Another object of the present invention is to provide a true fresh water desalination device capable of continuously reforming. The Mashimizu demineralizer according to the present invention is placed in restaurants, hotels, kitchens of general households to prepare water for cooking, drinking or ice making, or installed in an appropriate place such as an office building or a restaurant. It is suitable for applications such as making water for self-service beverages, and can also be combined with a refrigerator to make cold water.
【０００４】[0004]
上記目的を達成するため本考案は、揚水循環ポンプを配した架台の上または側 部に処理水受水タンクを設け、該処理水受水タンク内に前記揚水循環ポンプに接 続される原水取り入れ管の上端を開口させるとともに、処理水受水タンク内の水 位に応じて原水導管を開閉する制御弁を設け、前記揚水循環ポンプの吐出配管に はオゾン発生器と接続したエゼクタを介して反応器を接続し、該反応器の出口側 には積層ろ材を充填した造水器を接続し、該造水器の出口側を前記処理水受水タ ンクに接続し、処理水受水タンクの適所には処理水取出し部を設けたものである 。 前記反応器は、下端の出口部が造水器と接続し側壁にオゾン混合原水の取り 入れ部が接続された筒体と、板厚を貫くオゾン排出口を有し前記筒体の上端に着 脱可能に取付けられる蓋体と、上端面が蓋体と適度の距離を持つように筒体の出 口部に挿脱可能に取り付けられる内筒とを有していることが好ましい。 In order to achieve the above object, the present invention provides a treated water receiving tank on or at a side of a stand where a pumping circulation pump is arranged, and the raw water intake connected to the pumping circulation pump is provided in the treated water receiving tank. A control valve that opens the upper end of the pipe and opens and closes the raw water pipe according to the water level in the treated water receiving tank is provided, and the discharge pipe of the pumping circulation pump reacts via an ejector connected to an ozone generator. Connected to the treated water receiving tank, the outlet side of the reactor is connected to a fresh water generator filled with laminated filter media, and the outlet side of the fresh water generator is connected to the treated water receiving tank. A treated water extraction unit is provided in an appropriate place. The reactor has a cylinder with an outlet at the lower end connected to a fresh water generator, and a side wall to which a part for taking in ozone-mixed raw water is connected, and an ozone discharge port penetrating the plate thickness and attached to the upper end of the cylinder. It is preferable to have a lid that is detachably attached, and an inner cylinder that is detachably attached to the outlet of the tubular body so that the upper end surface has an appropriate distance from the lid.
【０００５】[0005]
以下本考案の実施例を添付図面に基いて説明する。 図１ないし図６は本考案による真清水造水装置の第１実施例一例を示しており 、 １は揚水循環ポンプ９と電源を内蔵した架台、２は処理水受水タンクであり 、この実施例では横断面三角状をなし、前記架台１上の半部に固定されている。 ３は反応器であり、処理水受水タンク２の頂面から延出し支柱部で支えられた支 台１０に固定されている。４は架台１に固定された造水器である。 前記処理水受水タンク２内には、図３と図６のように、下端がタンク底に達す る原水取り入れ管５が配されており、この原水取り入れ管５の上端開口に対応す る部位には、外部から原水導管(通常のばあい水道管)６の吐出部が導かれ、この 原水導管６の吐出部にはボール弁のような制御弁７が取り付けられ、この制御弁 ７による原水導管６の自動開閉によって処理水受水タンク内の水位を所定レベル に保つようにしている。 前記処理水受水タンク２の底部には原水取り入れ管５に通じる細径の導管８が 接続され、該導管８は先端が前記揚水循環ポンプ９の吸込み側に接続されている 。揚水ポンプ９の吐出配管９０は上方に立上り、エゼクタ１１を介して前記反応 器３に導かれている。導管８は揚水循環ポンプ９よりも上流側に処理水受水タン クの水を抜く排水弁８１が介装されている。 エゼクタ１１は、図４のように本管部１１０にオリフィス１１１を設けるとと もに、これよりも下流側にオゾン導入口１１２を設け、これにオゾン発生機１２ の導管を接続している。オゾン発生機１２は処理水受水タンク２の側壁あるいは 架台内など任意の部位に取り付けられる。 An embodiment of the present invention will be described below with reference to the accompanying drawings. 1 to 6 show an example of a first embodiment of a fresh water fresh water producing apparatus according to the present invention, 1 is a stand with a pumping circulation pump 9 and a power source built in, 2 is a treated water receiving tank, and this implementation In the example, the cross section has a triangular shape and is fixed to a half portion on the gantry 1. Reference numeral 3 denotes a reactor, which is fixed to a pedestal 10 which extends from the top surface of the treated water receiving tank 2 and is supported by a column. Reference numeral 4 denotes a fresh water generator fixed to the mount 1. As shown in FIGS. 3 and 6, a raw water intake pipe 5 whose lower end reaches the tank bottom is arranged in the treated water receiving tank 2, and a portion corresponding to an upper opening of the raw water intake pipe 5. A discharge part of a raw water conduit (usually a water pipe) 6 is introduced from the outside, and a control valve 7 such as a ball valve is attached to the discharge part of the raw water conduit 6 and the raw water by this control valve 7 is attached. The water level in the treated water receiving tank is maintained at a predetermined level by automatically opening and closing the conduit 6. At the bottom of the treated water receiving tank 2, a small-diameter conduit 8 communicating with the raw water intake pipe 5 is connected, and the end of the conduit 8 is connected to the suction side of the pumping circulation pump 9. A discharge pipe 90 of the pumping pump 9 rises upward and is guided to the reactor 3 via an ejector 11. A drain valve 81 for draining the water of the treated water receiving tank is installed upstream of the pump 8 in the conduit 8. As shown in FIG. 4, the ejector 11 is provided with an orifice 111 in the main pipe section 110 and an ozone inlet 112 downstream of the orifice 111, to which the conduit of the ozone generator 12 is connected. The ozone generator 12 is attached to an arbitrary part such as a side wall of the treated water receiving tank 2 or a mount.
【０００６】 反応器３は、図４のように支台１０に底板部３１をもって固定された筒体３０ と、該筒体３０の上端開口に着脱可能に取り付けられた蓋体３２と、下部外周の つば３３０を介して底板部３１の中央の出口部(開口)３１０に挿脱可能に嵌まる 内筒３３と、前記筒体３０の側方に設けたブラケットを介して保持された縦長の オゾン混合原水供給管３４とを有し、このオゾン混合原水供給管３４の上端に前 記エゼクタ１１の下流側が接続されている。 前記内筒３３は上端が開口し、この開口面と蓋体３２の下面との間に所要の空 間が形成されるような長さに設定されており、蓋体３２にはオゾンなどの気体成 分を外部に排出するオゾン排出口３２０が板厚を貫いて設けられている。また、 オゾン混合原水供給管３４は下端部が屈曲し、図５のように吐出口３４０が内筒 ３３の接線方向に開口するように筒体３０に挿着され、それにより内筒３３のま わりで上昇旋回流が創成されるようになっている。 反応器３の全部または少なくとも筒体３０と内筒３３はアクリル樹脂などによ って透明に構成されている。As shown in FIG. 4, the reactor 3 includes a tubular body 30 fixed to the abutment 10 with a bottom plate portion 31, a lid body 32 detachably attached to an upper end opening of the tubular body 30, and a lower outer periphery. A vertically long ozone that is retained via an inner cylinder 33 that is removably fitted into an outlet (opening) 310 at the center of the bottom plate portion 31 via a brim 330 and a bracket provided on the side of the cylindrical body 30. It has a mixed raw water supply pipe 34, and the downstream side of the ejector 11 is connected to the upper end of the ozone mixed raw water supply pipe 34. The inner cylinder 33 has an upper end opening, and is set to have a length such that a required space is formed between the opening surface and the lower surface of the lid 32. The lid 32 has a gas such as ozone. An ozone outlet 320 for discharging the components to the outside is provided through the plate thickness. Further, the lower end of the ozone-mixed raw water supply pipe 34 is bent, and as shown in FIG. 5, the discharge port 340 is inserted into the cylindrical body 30 so as to open in the tangential direction of the inner cylinder 33. Instead, a rising swirl flow is created. All or at least the cylindrical body 30 and the inner cylinder 33 of the reactor 3 are transparently made of acrylic resin or the like.
【０００７】 造水器４は図３のように上下を端板４０，４０’で塞がれた筒状のケーシング ４１と、これの内部に充填された積層ろ材４２を有し、積層ろ材４２の上下に対 応するケーシング内には端板４０，４０’との間に集水室４４，４４’を得るよ うに多孔板４３，４３’が張設されている。 前記積層ろ材４２は多量の無機塩類を含む活性石例えば麦飯石などの溶結凝灰 石、さらに好ましくは遠赤外線放射性能を持つ炭類たとえば備長炭などの白炭類 を併用する。井戸水などの場合には好気性菌による生物膜の定着しやすいろ過材 を使用してもよい。 前記反応器３の内筒３３の下端は導管１３によって造水器４の下側集水室４４ ’に接続されており、上側集水室４４は処理水導管１４によって処理水受水タン ク２に接続されている。この実施例においては処理水受水タンク２に取出し管１ ５が設けられ、手動開閉式または自動開閉式の弁１５０によって随時処理水を取 り出せるようになっている。As shown in FIG. 3, the water generator 4 has a cylindrical casing 41 whose upper and lower sides are closed by end plates 40 and 40 ′, and a laminated filter medium 42 filled inside the casing 41. In the casings corresponding to the upper and lower sides of the casing, perforated plates 43, 43 'are stretched so as to obtain water collecting chambers 44, 44' between the casing and the end plates 40, 40 '. For the laminated filter medium 42, activated stones containing a large amount of inorganic salts, such as welded tuff such as barley stone, and more preferably charcoal having far-infrared radiation performance, such as white charcoal such as Bincho charcoal, are used together. In the case of well water, you may use a filter that allows the aerobic bacteria to settle the biofilm. The lower end of the inner cylinder 33 of the reactor 3 is connected to the lower water collecting chamber 44 ′ of the fresh water generator 4 by the conduit 13, and the upper water collecting chamber 44 is connected to the treated water receiving tank 2 by the treated water conduit 14. It is connected to the. In this embodiment, the treated water receiving tank 2 is provided with a take-out pipe 15 so that the treated water can be taken out at any time by a valve 150 of a manual opening type or an automatic opening type.
【０００８】 そして、処理水受水タンク２内の水が取り出されないときにも絶えず処理水受 水タンク２内の水を循環浄化するため、原水取り入れ管５の下端周部には図６の ように処理水受水タンク２の底に開口する比較的小さな取出し穴５０を設け、ま た好ましくは原水取り入れ管５の上端部に設定水位よりも下にいたる長さのスリ ット状の上水取り込み部５１を設けている。 また、積層ろ材４２がコロイド状成分によって汚れた時に洗浄するため、上側 集水室４４には原水導管６と方向切換えバルブ１６０を介して接続した逆洗用配 管１６が導かれ、下側集水室４４’には逆洗用排水弁１７が接続されている。In order to constantly circulate and purify the water in the treated water receiving tank 2 even when the water in the treated water receiving tank 2 is not taken out, the raw water intake pipe 5 has a lower peripheral portion shown in FIG. As described above, a relatively small take-out hole 50 that opens at the bottom of the treated water receiving tank 2 is provided, and preferably, a slit-like top having a length that is below the set water level is provided at the upper end of the raw water intake pipe 5. A water intake section 51 is provided. Further, in order to wash the laminated filter medium 42 when it is contaminated by the colloidal components, the backwash pipe 16 connected to the raw water conduit 6 via the direction switching valve 160 is guided to the upper water collecting chamber 44, and the lower water collecting chamber 44 is guided. The backwash drain valve 17 is connected to the water chamber 44 '.
【０００９】 図７と図８は本考案の第２実施例を示している。 この実施例においては、処理水受水タンク２の上に密閉状の処理水戻し筒１８ を固定し、この処理水戻し筒１８に処理水導管１４を接続するとともに、処理水 戻し筒１８内に処理水受水タンク２内に伸びるオーバフロー式戻し管１８０を望 ませている。 また、積層ろ材４２の逆洗用配管１６がエゼクタ１１から造水器４にいたる系 の適所に方向切換えバルブ１６０を介して接続しされている。その他の構造は第 １実施例と同様である。 その他図面において、１９は処理水受水タンク２の頂部に設けた点検蓋、４５ は積層ろ材４２の点検・交換用の蓋である。 図示するものは本考案の一例であり、処理水受水タンク２は架台の側部に設け られていてもよい。また、処理水受水タンク２は外装型または内装型の冷凍機を 有していてもよく、取出し管１５があるいはこれと別の取出し管が製氷機に接続 されるようになっていてもよい。7 and 8 show a second embodiment of the present invention. In this embodiment, a sealed treated water return tube 18 is fixed on the treated water receiving tank 2, a treated water conduit 14 is connected to the treated water return tube 18, and a treated water return tube 18 is provided. An overflow type return pipe 180 that extends into the treated water receiving tank 2 is desired. Further, the backwashing pipe 16 of the laminated filter medium 42 is connected to a proper position in the system from the ejector 11 to the fresh water generator 4 through a direction switching valve 160. The other structure is similar to that of the first embodiment. In the other drawings, 19 is an inspection lid provided on the top of the treated water receiving tank 2, and 45 is an inspection / replacement lid for the laminated filter medium 42. What is shown is an example of the present invention, and the treated water receiving tank 2 may be provided on a side portion of the gantry. Further, the treated water receiving tank 2 may have an external or internal refrigerator, and the take-out pipe 15 or another take-out pipe may be connected to the ice making machine. .
【００１０】 実施例の作用を説明すると、原水導管６から原水を供給し、揚水循環ポンプ９ を駆動すれば、原水は原水導管６から処理水受水タンク２に内設されている原水 取り入れ管５に流入し、処理水受水タンク２外の導管８を介して揚水循環ポンプ ９に吸い込まれ、加圧されて吐出配管９０に圧送される。 吐出配管９にはエゼクタ１１が介在されており、原水はオリフィス１１１を通 過することによって流速が増し、それによりオゾン発生機１２で作られたオゾン が導入口１１２からジェット状に吸い込まれ、原水に混合される。このオゾン混 合原水は縦長のオゾン混合原水供給管３４を通過することによって旺盛に反応し 、次いで吐出口３４０から筒体３３に吹き込まれる。吐出口３４０は内筒３３の 接線方向に開口しているため旋回流となり、それによりオゾンと原水とが激しく 撹拌され十分に気液接触される。これによりオゾンの持つ強力な酸化作用で雑菌 類が滅菌され、また塩素やトリハロメタン等の塩素化合物類が分解され、同時に カルキ臭などの異臭が除去される。Explaining the operation of the embodiment, when raw water is supplied from the raw water conduit 6 and the pumping circulation pump 9 is driven, the raw water is fed from the raw water conduit 6 into the treated water receiving tank 2 through the raw water intake pipe. 5, it is sucked into the pumped water circulation pump 9 through the conduit 8 outside the treated water receiving tank 2, is pressurized, and is sent to the discharge pipe 90 under pressure. An ejector 11 is interposed in the discharge pipe 9, and the flow rate of the raw water increases as it passes through the orifice 111, whereby the ozone produced by the ozone generator 12 is sucked in a jet form from the inlet 112, and the raw water is discharged. Mixed in. The ozone-mixed raw water vigorously reacts by passing through the vertically long ozone-mixed raw water supply pipe 34, and then is blown into the cylindrical body 33 from the discharge port 340. Since the discharge port 340 opens in the tangential direction of the inner cylinder 33, it forms a swirling flow, whereby ozone and raw water are vigorously stirred and sufficiently brought into gas-liquid contact. As a result, ozone has a strong oxidative effect to sterilize various bacteria, decompose chlorine compounds such as chlorine and trihalomethane, and at the same time remove offensive odor such as chlorine.
【００１１】 上記のようにして除去された気体有害物質は残留オゾンともども内筒３３の上 端と蓋体３２の間の空間に集まり、オゾン排出口３２０から外部に放散される。 一方、酸化還元電位が与えられ、クラスターの小さくなった非腐食性の一次処理 水は、内筒３３の上端開口から内部を流下し、導管１３によって造水器４の下側 集水室４４’に導入される。上記したオゾンによる処理状態は反応器３を透明に することによって外部から目視することができ、合わせて動的美観を得ることが できる。 下側集水室４４’に供給された一次処理水は、多孔板４３’を通り、その上の 積層ろ材４２中を湧昇流となって上昇してゆく。積層ろ材４２はこの例では炭類 を有しており、これに一次処理水が接触することにより炭酸水素イオン等により 残留オゾンが分解され、同時に遠赤外線が照射されることにより還元浄化される 。さらに麦飯石の如き活性石と接触することにより、強い吸着力重金属、臭気、 殺菌類などが吸着分解され、また活性石に含まれる鉄、マグネシウム、マンガン 、カルシウムなどの各種無機塩類が溶出するためイオン化した活性水となり、同 時にＰＨが弱アルカリ(7.4程度)に調整される。これで安全で、ミネラル分の豊 かな処理水となる。 上記のようにして得られた処理水は上側集水室４４から処理水導管１４により 処理水受水タンク２に送り込まれ、この処理水の水位は制御弁７によって制御さ れ、設定した水位に達すると原水導管６からの原水の供給が停止され、取出し管 １５から処理水を任意に取り出すことができ、水位が低下すると原水導管６から 原水が処理水と分離された原水取り入れ管５に供給され、前記のように処理され る。The gaseous toxic substances removed as described above gather together with residual ozone in the space between the upper end of the inner cylinder 33 and the lid 32, and are diffused to the outside from the ozone discharge port 320. On the other hand, the non-corrosive primary treated water, which has been given an oxidation-reduction potential and has reduced clusters, flows down through the upper end opening of the inner cylinder 33, and is guided by the conduit 13 to the lower water collecting chamber 44 ′ of the fresh water generator 4. Will be introduced to. The above-mentioned treatment state with ozone can be visually observed from the outside by making the reactor 3 transparent, and a dynamic aesthetic appearance can also be obtained. The primary treated water supplied to the lower water collecting chamber 44 'passes through the perforated plate 43' and rises as an upwelling flow in the laminated filter medium 42 above it. The laminated filter medium 42 has charcoal in this example, and residual primary ozone is decomposed by hydrogen carbonate ions and the like when the primary treated water comes into contact with this, and at the same time, it is reduced and purified by being irradiated with far infrared rays. In addition, when it comes into contact with activated stones such as barley stone, it has strong adsorptive power. It becomes ionized active water, and at the same time, PH is adjusted to weak alkali (about 7.4). This is a safe, mineral-rich, treated water. The treated water obtained as described above is sent from the upper water collecting chamber 44 to the treated water receiving tank 2 through the treated water conduit 14, and the treated water level is controlled by the control valve 7 to the set water level. When it reaches, the supply of raw water from the raw water pipe 6 is stopped, the treated water can be taken out arbitrarily from the take-out pipe 15, and when the water level drops, the raw water is fed from the raw water pipe 6 to the raw water intake pipe 5 separated from the treated water. And processed as described above.
【００１２】 さらに本考案においては、原水取り入れ管５の下端部に比較的小さな取出し穴 ５０があり、原水取り入れ管５の上端部には設定水位よりも下に到る上水取り込 み部５１がある。このため、原水導管６からの原水の供給が停止された状態にお いても、揚水循環ポンプ９の継続的駆動で処理水受水タンク２内の底域の水は取 出し穴５０から導管８に吸い込まれ、また上水は上水取り込み部５１から原水取 り入れ管５に流入し導管８に吸い込まれ、揚水循環ポンプ９から吐出配管９０を 介してエゼクタ１１に到り、前記した系統によって処理され、上側集水室４４か ら処理水導管１４により処理水受水タンク２に送り込まれる循環系が構成される 。 このため、処理水受水タンク２の処理水は絶えず流動しつつ短時間で一時処 理、二次処理され、処理水受水タンク２の底にコロイド等が全く沈殿することが ない。Further, in the present invention, there is a relatively small take-out hole 50 at the lower end of the raw water intake pipe 5, and at the upper end of the raw water intake pipe 5 there is a clean water intake 51 that is below the set water level. There is. Therefore, even when the supply of the raw water from the raw water conduit 6 is stopped, the water in the bottom area of the treated water receiving tank 2 is continuously driven by the pumping circulation pump 9 from the extraction hole 50 to the conduit 8 In addition, the clean water flows into the raw water intake pipe 5 from the clean water intake part 51, is sucked into the conduit 8, reaches the ejector 11 from the pumping circulation pump 9 through the discharge pipe 90, and is discharged by the system described above. A circulation system that is processed and is sent from the upper water collection chamber 44 to the treated water receiving tank 2 by the treated water conduit 14 is configured. For this reason, the treated water in the treated water receiving tank 2 is constantly processed and secondarily treated in a short time while constantly flowing, and colloids and the like do not precipitate at the bottom of the treated water receiving tank 2.
【００１３】 前記のように積層ろ材４２の活性石が塩素や不純物を吸着することから、ろ材 細間やろ材表面にコロイド状成分が堆積する。第1実施例の場合、揚水循環ポン プ９の駆動を一時止め、逆洗用排水弁１７を開放し、方向切換えバルブ１６０を 逆洗側に切り替える。こうすれば、原水が造水器４の上側集水室４４に送られ、 積層ろ材４２を通って下側集水室４４’に流下し、逆洗用排水弁１７から排出さ れるため、積層ろ材４２の汚れが流れ落される。 第２実施例においては、揚水循環ポンプ９の駆動を一時止め、逆洗用排水弁１ ７を開放し、方向切換えバルブ１６０を逆洗側に切り替え、揚水循環ポンプ９を 駆動すれば、オゾン混合水が上側集水室４４に圧流され下側集水室４４’から流 出するため、積層ろ材４２の汚れが流れ落される。このようにして洗浄が終わっ たならば、逆洗用排水弁１７を閉じ、方向切換えバルブ１６０を通常循環系に切 り替えればよい。As described above, since the activated stone of the laminated filter medium 42 adsorbs chlorine and impurities, colloidal components are deposited on the filter medium spaces and the surface of the filter medium. In the case of the first embodiment, the drive of the pumping circulation pump 9 is temporarily stopped, the backwash drain valve 17 is opened, and the direction switching valve 160 is switched to the backwash side. In this way, the raw water is sent to the upper water collecting chamber 44 of the fresh water generator 4, flows through the laminated filter media 42 into the lower water collecting chamber 44 ′, and is discharged from the backwash drain valve 17. The dirt of the filter material 42 is washed away. In the second embodiment, the driving of the pumping water circulation pump 9 is temporarily stopped, the backwash drain valve 17 is opened, the direction switching valve 160 is switched to the backwashing side, and the pumping water circulation pump 9 is driven to mix ozone. Since the water is pressure-fed to the upper water collecting chamber 44 and flows out from the lower water collecting chamber 44 ', the dirt on the laminated filter medium 42 is washed off. When the washing is completed in this way, the backwash drain valve 17 may be closed and the direction switching valve 160 may be switched to the normal circulation system.
【００１４】 また、蓋体３２が筒体３０に対して取り外すことができ、しかも内筒３３が筒 体３０から抜き出すことができるため、反応器３が汚れたり、内筒３３上方の空 間に泡状の汚濁物質が溜っても、簡単に清掃等を行うことができる。しかも、内 筒３３を抜き出しても、筒体３０に吹き込まれた水は開口３１０から流出するた め、運転を止めずに清掃等を行うことができる。Further, since the lid body 32 can be removed from the cylinder body 30 and the inner cylinder 33 can be pulled out from the cylinder body 30, the reactor 3 becomes dirty, or the space above the inner cylinder 33 is emptied. Even if foamy pollutants are accumulated, cleaning or the like can be easily performed. Moreover, even if the inner cylinder 33 is pulled out, the water blown into the cylindrical body 30 flows out through the opening 310, so that cleaning or the like can be performed without stopping the operation.
【００１５】[0015]
以上説明した本考案によるときには、コンパクトな構造で、水道水を安全でし かも天然の涌き水のようなうまい水に連続的に改質しつつ貯蔵することができる というすぐれた効果が得られる。 According to the present invention described above, it is possible to obtain an excellent effect that tap water has a compact structure and can be stored while being continuously reformed into delicious water such as natural sprinkling water.
【図１】本考案の第１実施例を示す斜視図である。FIG. 1 is a perspective view showing a first embodiment of the present invention.
【図２】第１実施例の実施例の系統図である。FIG. 2 is a system diagram of an embodiment of the first embodiment.
【図３】第１実施例の部分切欠分解斜視図である。FIG. 3 is a partially cutaway exploded perspective view of the first embodiment.
【図４】第１実施例における反応器の断面図である。FIG. 4 is a sectional view of a reactor in the first embodiment.
【図５】図４の横断面図である。5 is a cross-sectional view of FIG.
【図６】第１実施例の処理水受水タンクの縦断側面図で
ある。FIG. 6 is a vertical sectional side view of the treated water receiving tank according to the first embodiment.
【図７】本考案の第２実施例を示す斜視図である。FIG. 7 is a perspective view showing a second embodiment of the present invention.
【図８】第２実施例の系統図である。FIG. 8 is a system diagram of a second embodiment.
１ 架台 ２ 処理水受水タンク ３ 反応器 ４ 造水器 ５ 原水取り入れ管 ６ 原水導管 ７ 制御弁 ９ 揚水循環ポンプ １１ エゼクタ １６ 逆洗用配管 １７ 逆洗用排水弁 １２ オゾン発生機 ３０ 筒体 ３２ 蓋体 ３３ 内筒 ４２ 積層ろ材 ４４，４４’ 集水室 ５０ 取出し穴 ５１ 上水取り込み部 ３１０ 出口部 ３２０ オゾン排出口 1 cradle 2 treated water receiving tank 3 reactor 4 fresh water generator 5 raw water intake pipe 6 raw water conduit 7 control valve 9 pumping circulation pump 11 ejector 16 backwash pipe 17 backwash drain valve 12 ozone generator 30 cylinder 32 Lid 33 Internal cylinder 42 Laminated filter media 44, 44 'Water collection chamber 50 Outlet hole 51 Clean water intake part 310 Outlet part 320 Ozone discharge port
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【手続補正書】[Procedure amendment]
【提出日】平成５年１０月８日[Submission date] October 8, 1993
【手続補正１】[Procedure Amendment 1]
【補正対象書類名】図面[Document name to be corrected] Drawing
【補正対象項目名】図２[Name of item to be corrected] Figure 2
【補正方法】変更[Correction method] Change
【補正内容】[Correction content]
【図２】 [Fig. 2]
【手続補正２】[Procedure Amendment 2]
【補正対象書類名】図面[Document name to be corrected] Drawing
【補正対象項目名】図４[Name of item to be corrected] Fig. 4
【補正方法】変更[Correction method] Change
【補正内容】[Correction content]
【図４】 [Figure 4]
【手続補正３】[Procedure 3]
【補正対象書類名】図面[Document name to be corrected] Drawing
【補正対象項目名】図５[Name of item to be corrected] Figure 5
【補正方法】変更[Correction method] Change
【補正内容】[Correction content]
【図５】 [Figure 5]
【手続補正４】[Procedure amendment 4]
【補正対象書類名】図面[Document name to be corrected] Drawing
【補正対象項目名】図６[Name of item to be corrected] Figure 6
【補正方法】変更[Correction method] Change
【補正内容】[Correction content]
【図６】 [Figure 6]
【手続補正５】[Procedure Amendment 5]
【補正対象書類名】図面[Document name to be corrected] Drawing
【補正対象項目名】図７[Name of item to be corrected] Figure 7
【補正方法】変更[Correction method] Change
【補正内容】[Correction content]
【図７】 [Figure 7]
【手続補正６】[Procedure correction 6]
【補正対象書類名】図面[Document name to be corrected] Drawing
【補正対象項目名】図８[Correction target item name] Figure 8
【補正方法】変更[Correction method] Change
【補正内容】[Correction content]
【図８】 [Figure 8]
Claims (6)
は側部に処理水受水タンク２を設け、該処理水受水タン
ク２内に前記揚水循環ポンプ９に接続される原水取り入
れ管５の上端を開口させるとともに、処理水受水タンク
２内の水位に応じて原水導管６を開閉する制御弁７を設
け、前記揚水循環ポンプ９の吐出配管９０にはオゾン発
生器１２と接続したエゼクタ１１を介して反応器３を接
続し、該反応器３の出口側には積層ろ材４２を充填した
造水器４を接続し、該造水器４の出口側を前記処理水受
水タンク２に接続し、処理水受水タンク２の適所には処
理水取出し部を設けたことを特徴とする真清水造水装
置。1. A treated water receiving tank 2 is provided on or on a side of a base 1 on which a pumping circulation pump 9 is arranged, and a raw water intake pipe connected to the pumping circulation pump 9 in the treated water receiving tank 2. A control valve 7 is provided which opens the upper end of 5 and opens and closes the raw water conduit 6 according to the water level in the treated water receiving tank 2, and a discharge pipe 90 of the pumping circulation pump 9 is connected to an ozone generator 12. The reactor 3 is connected via the ejector 11, and the outlet side of the reactor 3 is connected to the fresh water generator 4 filled with the laminated filter medium 42, and the outlet side of the fresh water generator 4 is connected to the treated water receiving tank. 2. A fresh water fresh water producing apparatus, characterized in that it is connected to 2 and a treated water take-out section is provided at an appropriate position of the treated water receiving tank 2.
ている請求項１に記載の真清水造水装置。2. The fresh water desalination apparatus according to claim 1, wherein the treated water receiving tank 2 has a triangular cross section.
続し側壁にオゾン混合原水の吹込み部が接続された筒体
３０と、板厚を貫くオゾン排出口３２０を有し前記筒体
３０の上端に着脱可能に取付けられる蓋体３２と、上端
面が蓋体３２と適度の距離を持つように筒体３０の出口
部３１０に挿脱可能に取り付けられる内筒３３とを有し
ている請求項１に記載の真清水造水装置。3. The reactor 3 has a cylindrical body 30 having an outlet at the lower end connected to the fresh water generator 4 and a side wall to which a blow-in portion of the raw water containing ozone is connected, and an ozone discharge port 320 penetrating the plate thickness. A lid 32 detachably attached to the upper end of the tubular body 30, and an inner tube 33 detachably attached to the outlet 310 of the tubular body 30 so that the upper end surface has an appropriate distance from the lid 32. The fresh water fresh water generator according to claim 1, which further comprises:
で作られている請求項３に記載の真清水造水装置。4. The fresh water fresh water generator according to claim 3, wherein at least the cylindrical body 30 and the inner cylinder 33 are made of a transparent material.
外底に接続した導管８に通じており、かつ原水取り入れ
管５の下端周部に処理水受水タンク２の低域に通じる取
出し穴５０を有している請求項１または請求項３に記載
の真清水造水装置。5. The raw water intake pipe 5 communicates with a conduit 8 connected to the outer bottom of the treated water receiving tank 2, and the lower end peripheral portion of the raw water intake pipe 5 communicates with a low region of the treated water receiving tank 2. The fresh water fresh water generator according to claim 1 or 3, which has an extraction hole 50.
４，４４’を有し、下側集水室４４に逆洗用排水弁１７
が接続され、上側集水室４４には逆洗用配管１６が接続
されているものを含む請求項１ないし５のいずれかに記
載の真清水造水装置。6. A fresh water generator 4 is provided above and below a laminated filter medium 42 to collect water.
4, 44 ', and the backwash drain valve 17 is provided in the lower water collecting chamber 44.
6. The fresh water fresh water generator according to any one of claims 1 to 5, further comprising a backwash pipe 16 connected to the upper water collecting chamber 44.
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| JP4320393U JPH079493U (en) | 1993-07-13 | 1993-07-13 | Mashimizu Demineralizer |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| JP4320393U JPH079493U (en) | 1993-07-13 | 1993-07-13 | Mashimizu Demineralizer |
Publications (1)
| Publication Number | Publication Date |
|---|---|
| JPH079493U true JPH079493U (en) | 1995-02-10 |
Family
ID=12657378
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| JP4320393U Pending JPH079493U (en) | 1993-07-13 | 1993-07-13 | Mashimizu Demineralizer |
Country Status (1)
| Country | Link |
|---|---|
| JP (1) | JPH079493U (en) |
Cited By (1)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| JP2006239480A (en) * | 2005-02-28 | 2006-09-14 | Yunifiido Engineering:Kk | Active hydrogen-containing water and its production method |
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|---|---|---|---|---|
| JPS6242791A (en) * | 1985-08-16 | 1987-02-24 | Meisui Giken Kk | Mineralized water making device |
| JPH01215396A (en) * | 1988-02-23 | 1989-08-29 | Senichi Masuda | Ozone water producing device |
| JPH02172593A (en) * | 1988-12-26 | 1990-07-04 | Plant Service:Kk | Apparatus for continuously supplying ozone water |
| JPH03293094A (en) * | 1990-04-09 | 1991-12-24 | Sankaino Chinmi:Kk | Water purifying device |
| JPH0615282A (en) * | 1992-06-30 | 1994-01-25 | J C Ii Eng:Kk | Water purifying apparatus |
-
1993
- 1993-07-13 JP JP4320393U patent/JPH079493U/en active Pending
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| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| JPS6242791A (en) * | 1985-08-16 | 1987-02-24 | Meisui Giken Kk | Mineralized water making device |
| JPH01215396A (en) * | 1988-02-23 | 1989-08-29 | Senichi Masuda | Ozone water producing device |
| JPH02172593A (en) * | 1988-12-26 | 1990-07-04 | Plant Service:Kk | Apparatus for continuously supplying ozone water |
| JPH03293094A (en) * | 1990-04-09 | 1991-12-24 | Sankaino Chinmi:Kk | Water purifying device |
| JPH0615282A (en) * | 1992-06-30 | 1994-01-25 | J C Ii Eng:Kk | Water purifying apparatus |
Cited By (1)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| JP2006239480A (en) * | 2005-02-28 | 2006-09-14 | Yunifiido Engineering:Kk | Active hydrogen-containing water and its production method |
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