JP5011419B2 - High water pressure water purification system - Google Patents

High water pressure water purification system Download PDF

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JP5011419B2
JP5011419B2 JP2010107078A JP2010107078A JP5011419B2 JP 5011419 B2 JP5011419 B2 JP 5011419B2 JP 2010107078 A JP2010107078 A JP 2010107078A JP 2010107078 A JP2010107078 A JP 2010107078A JP 5011419 B2 JP5011419 B2 JP 5011419B2
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雄介 松下
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ショウワ洗浄機株式会社
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本発明は、より長時間にわたり連続浄水運転可能で、かつ低コストの高水圧浄水装置に関する。   The present invention relates to a high-pressure water purification apparatus that can perform continuous water purification operation for a longer time and is low in cost.

液体サイクロンを利用して廃水を浄化する技術として、例えば特許文献1記載の廃水浄化設備が知られている。   As a technique for purifying wastewater using a liquid cyclone, for example, a wastewater purification facility described in Patent Document 1 is known.

この廃水浄化設備において、雨水、生活廃水等の原水は、一次濾過箱内のごみ除去スクリーンを通過した後、液体サイクロン装置に供給され、さらに三次濾過室内の浄化マット及び殺菌マットで濾過される。これにより、原水が清浄な水に浄化される。   In this wastewater purification facility, raw water such as rainwater and domestic wastewater passes through a dust removal screen in the primary filtration box, is then supplied to the liquid cyclone device, and is further filtered by a purification mat and a sterilization mat in the tertiary filtration chamber. Thereby, the raw water is purified to clean water.

特開2000−135500号公報JP 2000-135500 A

ところで、不純物を含む原水を液体サイクロン内で十分な速度で旋回させるためには、液体サイクロンに原水を高圧で送り込む高性能なポンプが必要となる。このため、その分、製造コストが高くなる。   By the way, in order to rotate the raw water containing impurities at a sufficient speed in the liquid cyclone, a high-performance pump that feeds the raw water into the liquid cyclone at a high pressure is required. For this reason, the manufacturing cost increases accordingly.

また、上記従来の廃水浄化設備は、例えば三次濾過層内の浄化マットの目詰まりによって濾過能力が低下する可能性がある。このため、定期的に濾過を中断して、濾過能力を再生するための逆洗浄が行う必要がある。   Moreover, the conventional wastewater purification equipment may have a reduced filtration capacity due to, for example, clogging of the purification mat in the tertiary filtration layer. For this reason, it is necessary to periodically stop the filtration and perform back washing to regenerate the filtration capacity.

本発明は上記事情に鑑みてなされたものであり、本発明の目的は、より長時間にわたり連続浄水運転可能な高水圧浄水装置をより低コストで提供することにある。   The present invention has been made in view of the above circumstances, and an object of the present invention is to provide a high-pressure water purification apparatus capable of continuous water purification operation for a longer time at a lower cost.

上記課題を解決するために、本発明においては、浄水槽に収容された液体サイクロンに、原水を供給しながら、オゾンガスを含む気泡を巻き込んだ水流を原水よりも高圧で噴射する。さらに、浄水槽の内部を仕切るフィルタを設けて、液体サイクロン側から、このフィルタに対して、オゾンガスを含む気泡を巻き込んだ水流を、原水よりも高圧で噴射する。   In order to solve the above-mentioned problem, in the present invention, while supplying raw water to a hydrocyclone accommodated in a water purification tank, a water flow including bubbles containing ozone gas is injected at a higher pressure than the raw water. Furthermore, the filter which partitions off the inside of a water purification tank is provided, and the water flow in which the bubble containing ozone gas was injected with respect to this filter from the liquid cyclone side at a pressure higher than raw | natural water.

例えば、本発明は、処理対象水から異物を除去する高水圧浄水装置であって、
原水供給口及び高圧水流供給口を有する液体サイクロンを収容し、当該液体サイクロンの下端開口部からのアンダーフローを貯水する浄水槽と、
前記浄水槽から溢れ出る、前記液体サイクロンの上端開口部からのオーバーフローが流入する排水路と、
前記処理対象水を前記原水供給口から前記液体サイクロンの内部に供給する処理対象供給手段と、
前記高圧水流供給口に取り付けられた第一のエジェクタノズルを有し、オゾンガスを含む気泡を巻き込んだ水流を、前記第一のエジェクタノズルから、前記液体サイクロンの内部に、前記液体サイクロンの内周方向に、前記処理対象水よりも高圧で噴射するジェット水流噴射手段と、を有する。
For example, the present invention is a high water pressure water purification device that removes foreign matter from water to be treated,
A water purification tank that contains a liquid cyclone having a raw water supply port and a high-pressure water flow supply port, and stores underflow from the lower end opening of the liquid cyclone,
A drainage channel overflowing from the water purification tank, into which overflow from the upper end opening of the hydrocyclone flows;
Processing target supply means for supplying the processing target water from the raw water supply port to the inside of the hydrocyclone;
A first ejector nozzle attached to the high-pressure water flow supply port, and a water flow including bubbles containing ozone gas is introduced from the first ejector nozzle into the liquid cyclone in the inner circumferential direction of the liquid cyclone. And jet water jetting means for jetting at a higher pressure than the water to be treated.

このような高水圧浄水装置において、
前記浄水槽の内部を、前記液体サイクロンを含む第一の室と前記液体サイクロンを含まない第二の室とに仕切るフィルタをさらに有し、
前記ジェット水流噴射手段は、
前記フィルタを介して前記第二の室側に向けられた第二のエジェクタノズルをさらに有し、オゾンガスを含む気泡を巻き込んだ水流を、さらに、前記第二のエジェクタノズルから前記フィルタに向けて噴射するようにしてもよい。
In such a high water pressure water purification device,
A filter that partitions the interior of the water purification tank into a first chamber containing the liquid cyclone and a second chamber not containing the liquid cyclone;
The jet water flow injection means
A second ejector nozzle directed to the second chamber side through the filter is further provided, and a water flow including bubbles containing ozone gas is further injected from the second ejector nozzle toward the filter. You may make it do.

本発明によれば、より長時間にわたり連続浄水運転可能な高水圧浄水槽をより低コストで実現することができる。   ADVANTAGE OF THE INVENTION According to this invention, the high-pressure-pressure water purification tank which can perform continuous water purification operation over a longer time is realizable at lower cost.

図1(A)は、本発明の一実施の形態に係る濾過システムの概略構成図であり、図1(B)は、図1(A)に示す高水圧浄水ユニット2の全体構成を説明するための図である。FIG. 1 (A) is a schematic configuration diagram of a filtration system according to an embodiment of the present invention, and FIG. 1 (B) illustrates the overall configuration of the high water pressure water purification unit 2 shown in FIG. 1 (A). FIG. 図2(A)は、図1(B)の高水圧浄水ユニット2に含まれる浄水槽22の上面図であり、図2(B)は、気泡群を含む高圧のジェット水流の噴射によって、フィルタからケーキが除去される様子を概念的に示した図である。2A is a top view of the water purification tank 22 included in the high water pressure water purification unit 2 of FIG. 1B, and FIG. 2B is a filter by jetting a high-pressure jet water stream containing bubbles. It is the figure which showed notionally the mode that the cake was removed from.

以下、本発明の一実施の形態について説明する。   Hereinafter, an embodiment of the present invention will be described.

まず、本実施の形態に係る濾過システムの全体構成について説明する。   First, the overall configuration of the filtration system according to the present embodiment will be described.

図1(A)に、本実施の形態に係る濾過システムの概略構成を示す。   FIG. 1A shows a schematic configuration of a filtration system according to this embodiment.

図示するように、本実施の形態に係る濾過システムには、原水タンクからの原水(井水、潅水、排水等)W1が供給される前処理ユニット1と、前処理ユニット1の後段に連結される高水圧浄水ユニット2と、を有する。なお、最終的な濾過水に要求される水質に応じて、高水圧浄水ユニット2の後段に、高水圧浄水ユニット2で濾過された濾過水W5をさらに高度濾過する高度濾過ユニット(限外濾過膜(UF)、ナノ濾過膜(NF)、逆浸透膜(RO)等)を連結してもよい。   As shown in the figure, the filtration system according to the present embodiment is connected to a pretreatment unit 1 to which raw water (well water, irrigation, drainage, etc.) W1 from a raw water tank is supplied, and a subsequent stage of the pretreatment unit 1. High water pressure water purification unit 2. In addition, according to the water quality required for the final filtered water, an advanced filtration unit (ultrafiltration membrane) that further filters the filtered water W5 filtered by the high water pressure water purification unit 2 after the high water pressure water purification unit 2 (UF), nanofiltration membrane (NF), reverse osmosis membrane (RO), etc.) may be connected.

前処理ユニット1は、原水タンクから原水W1を送り出す原水供給ポンプ(不図示)と、原水供給ポンプにより供給される原水W1から粗大懸濁物質(SS)を除去するウエッジスクリーン除塵装置11と、を有する。また、ウエッジスクリーン除塵装置11は、貯水タンク111と、一端(以下、上端)側よりも他端(以下、下端)側が低くなるように貯水タンク111上に斜めにかけ渡されたウエッジスクリーン112と、ウエッジスクリーン112の下端側に配置されたSS収集タンク113と、を有する。   The pretreatment unit 1 includes a raw water supply pump (not shown) that feeds the raw water W1 from the raw water tank, and a wedge screen dust removal device 11 that removes coarse suspended solids (SS) from the raw water W1 supplied by the raw water supply pump. Have. In addition, the wedge screen dust removing device 11 includes a water storage tank 111, a wedge screen 112 that is slanted over the water storage tank 111 so that the other end (hereinafter, lower end) side is lower than the one end (hereinafter, upper end) side, And an SS collection tank 113 disposed on the lower end side of the wedge screen 112.

このような前処理ユニット1において、原水供給ポンプからの原水W1がウエッジスクリーン112の上端側からウエッジスクリーン上面に供給されると、ウエッジスクリーン112を通過した一次濾過水(粗大懸濁物質が除去された水)W2が貯水タンク111に蓄えられる。また、ウエッジスクリーン上面を残りの原水W1とともに流れ落ちた粗大懸濁物質(SS)が、SS収集タンク113に排出される。   In such a pretreatment unit 1, when the raw water W1 from the raw water supply pump is supplied to the upper surface of the wedge screen 112 from the upper end side of the wedge screen 112, the primary filtered water (coarse suspended solids that have passed through the wedge screen 112 is removed). Water) W2 is stored in the water storage tank 111. Further, the coarse suspended matter (SS) that has flowed down along with the remaining raw water W <b> 1 on the upper surface of the wedge screen is discharged to the SS collection tank 113.

一方、高水圧浄水ユニット2は、濾過運転開始時に清水が満たされる浄水槽22と、ウエッジスクリーン除塵装置11の貯水タンク111から一次濾過水W2を低圧で浄水槽22に送り出す低圧ポンプ21と、オゾンガスAを含む気泡群を巻き込んだジェット水流W4を高圧で浄水槽22内に噴射するジェット水流噴射装置23と、を有する。   On the other hand, the high water pressure water purification unit 2 includes a water purification tank 22 that is filled with fresh water at the start of filtration operation, a low pressure pump 21 that sends the primary filtrate W2 from the water storage tank 111 of the wedge screen dust remover 11 to the water purification tank 22 at a low pressure, and ozone gas. A jet water flow injection device 23 that injects a jet water flow W4 including bubbles including A into the water purification tank 22 at a high pressure.

図1(B)に、高水圧浄水ユニット2の概略構造を示し、図2(A)に、浄水槽22の上面図を示す。なお、図1(B)及び図2(A)においては、浄水槽22に対して、深さ方向をZ方向、幅方向をX方向、長さ方向をY方向と定義している。   FIG. 1B shows a schematic structure of the high water pressure water purification unit 2, and FIG. 2A shows a top view of the water purification tank 22. In addition, in FIG. 1 (B) and FIG. 2 (A), with respect to the water purification tank 22, the depth direction is defined as the Z direction, the width direction is defined as the X direction, and the length direction is defined as the Y direction.

図示するように、浄水槽22の内部には、濾過精度の異なる2枚のフィルタ(荒目フィルタ225A、細目フィルタ225B)と、両端部(下端部、上端部)が開口された2本の液体サイクロン226と、が収容されている。また、浄水槽22のY方向側壁各々の外部に、対向するY方向側壁の縁に沿って排水口付き排水路224が設けられている。   As shown in the drawing, inside the water purification tank 22, two filters (coarse filter 225A, fine filter 225B) having different filtration accuracy and two liquids having both ends (lower end and upper end) opened. And a cyclone 226 is accommodated. Moreover, the drainage channel 224 with a drain outlet is provided in the exterior of each Y direction side wall of the water purification tank 22 along the edge of the opposing Y direction side wall.

浄水槽22の内部は、2枚のフィルタ225A、225Bにより、Y方向に連続した3つの室(一方のX方向側壁と荒目フィルタ225Aとの間の遠心分離室221、荒目フィルタ225Aと細目フィルタ225Bとの間の濾過室222、細目フィルタ225Bと他方のX方向側壁との間の貯水室223)に仕切られている。各室221〜223の底面には、それぞれ、浄水槽22内の水を抜くための出水口221A、222A、223Aが設けられている。   The interior of the water purification tank 22 is divided into three chambers (a centrifugal separation chamber 221 between one side wall in the X direction and the coarse filter 225A, the coarse filter 225A, and the fine filter by two filters 225A and 225B. It is partitioned into a filtration chamber 222 between the filter 225B and a water storage chamber 223) between the fine filter 225B and the other side wall in the X direction. Water outlets 221A, 222A, and 223A for draining water from the water purification tank 22 are provided on the bottom surfaces of the chambers 221 to 223, respectively.

2本の液体サイクロン226は、遠心分離室221に、下端側の開口部(アンダーフロー口)2261を浄水槽22の底面に向けた状態でX方向に並べられて配置される。各液体サイクロン226には、低圧ポンプ21の出水口に接続される一次濾過水供給口2262とは別に、ジェット水流噴射装置23のエジェクタノズル(後述)が接続されるジェット水流供給口2263が設けられており、浄水槽22の底面に面したアンダーフロー口2261に近づくにしたがって徐々に内径が狭くなるように、一次濾過水供給口2262及びジェット水流供給口2263よりも低位置からテーパがつけられている。また、各液体サイクロン226の上端側の開口部(オーバーフロー口)2264からのオーバーフローF1が遠心分離室221内の水面付近の水とともに排水路224へ溢れ出るように、各液体サイクロン226のオーバーフロー口2264は、浄水槽22のY方向側壁よりも適当な距離だけZ方向に低い位置に設けられている。   The two hydrocyclones 226 are arranged in the centrifuge chamber 221 in the X direction with the lower end opening (underflow port) 2261 facing the bottom surface of the water purification tank 22. Each hydrocyclone 226 is provided with a jet water flow supply port 2263 to which an ejector nozzle (described later) of the jet water flow injection device 23 is connected, in addition to the primary filtrate water supply port 2262 connected to the water outlet of the low pressure pump 21. It is tapered from a lower position than the primary filtrate water supply port 2262 and the jet water flow supply port 2263 so that the inner diameter gradually decreases as it approaches the underflow port 2261 facing the bottom surface of the water purification tank 22. Yes. Moreover, the overflow port 2264 of each hydrocyclone 226 is overflowed so that the overflow F1 from the opening (overflow port) 2264 on the upper end side of each hydrocyclone 226 overflows into the drainage channel 224 together with water near the water surface in the centrifugal separation chamber 221. Is provided at a position lower in the Z direction by an appropriate distance than the Y direction side wall of the water purification tank 22.

ジェット水流噴射装置23は、適当な濃度のオゾンガスAを発生するオゾン発生器231と、清水タンクから清水W3を高圧(例えば約8Mpa)で送り出す高圧ポンプ232と、オゾン発生器231からのオゾンガスA及び高圧ポンプ232からの清水W3が送り込まれるエジェクタノズル233群と、を有している。   The jet water jetting device 23 includes an ozone generator 231 that generates ozone gas A having an appropriate concentration, a high-pressure pump 232 that pumps fresh water W3 from a fresh water tank at a high pressure (for example, about 8 Mpa), and ozone gas A from the ozone generator 231 and And an ejector nozzle 233 group into which fresh water W3 from the high-pressure pump 232 is fed.

ここで、エジェクタノズル233は、絞り付近で、高圧ポンプ232から高圧で送り込まれる清水W3に、オゾン発生器231からのオゾンガスAを混入させ、これにより、殺菌、脱臭、脱色作用を有するオゾンガスAを含む気泡群を巻き込んだジェット水流W4を吐出口から噴射する(図2(B)参照)。このようなエジェクタノズル233のうち、2つのエジェクタノズル233は、各液体サイクロン226のジェット水流供給口2263に接続される。また、その他のエジェクタノズル233は、一部が遠心分離室221内の水を濾過室222に圧送するように荒目フィルタ225Aに向けてX方向に配列され、残りが濾過室222内の水を貯水室223に圧送するように細目フィルタ225Bに向けてX方向に配列される。なお、遠心分離室221内及び濾過室222内のエジェクタノズル233列は、オゾンガスAを含む気泡群を巻き込んだジェット水流W4が水中で圧力を保ちながらフィルタ225A、225Bを通過可能な水深で、かつ浄水槽22内の水が比較的清浄な位置(例えば、水深の浅い位置)に配置されていることが望ましい。   Here, the ejector nozzle 233 mixes the ozone gas A from the ozone generator 231 in the fresh water W3 fed at a high pressure from the high pressure pump 232 in the vicinity of the throttle so that the ozone gas A having a sterilizing, deodorizing, and decolorizing action is mixed. A jet water stream W4 including a bubble group including the liquid is ejected from the discharge port (see FIG. 2B). Of the ejector nozzles 233, two ejector nozzles 233 are connected to the jet water flow supply ports 2263 of the respective hydrocyclones 226. Further, the other ejector nozzles 233 are arranged in the X direction toward the coarse filter 225A so that a part of the water in the centrifugal separation chamber 221 is pumped to the filtration chamber 222, and the rest are used for the water in the filtration chamber 222. They are arranged in the X direction toward the fine filter 225B so as to be pumped to the water storage chamber 223. The rows of ejector nozzles 233 in the centrifugal separation chamber 221 and the filtration chamber 222 have a depth of water that allows the jet water flow W4 including the bubbles including the ozone gas A to pass through the filters 225A and 225B while maintaining the pressure in the water. It is desirable that the water in the water purification tank 22 is disposed at a relatively clean position (for example, a shallow position).

このような高水圧浄水ユニット2において、浄水槽22に清水を満たしてから、低圧ポンプ21、オゾン発生器231及び高圧ポンプ232を駆動すると、遠心分離室221内の水に浸された各液体サイクロン226の内部に、一次濾過水W2が低圧で供給されるとともに、オゾンガスAを含む気泡群を巻き込んだ高圧のジェット水流W4が液体サイクロン226の内周方向に噴射される。これにより、異物を含む一次濾過水W2が高圧のジェット水流W4とともに各液体サイクロン226の内部で旋回するため、比重の小さい油等の異物を含むオーバーフローF1が、オーバーフロー口2264から旋回しながら溢れ出して、遠心分離室221内の水面付近の水とともに浄水槽22のY方向両側壁の外部に設けられた排水路224に排出される。一方、比重の大きな異物を含むアンダーフローF2がアンダーフロー口2261から遠心分離室221内の水中に放出されるが、比重の大きな異物は遠心分離室221の底面に沈殿するため、遠心分離室221内の上部には、オゾンガスAで殺菌・脱脱臭等された清浄な水が残留する。   In such a high water pressure water purification unit 2, when the water purification tank 22 is filled with fresh water and then the low pressure pump 21, the ozone generator 231 and the high pressure pump 232 are driven, each liquid cyclone immersed in the water in the centrifugal separation chamber 221. The primary filtered water W <b> 2 is supplied into the interior of 226 at a low pressure, and a high-pressure jet water flow W <b> 4 involving bubbles including the ozone gas A is jetted in the inner circumferential direction of the hydrocyclone 226. As a result, the primary filtered water W2 containing foreign matter swirls inside each hydrocyclone 226 together with the high-pressure jet water flow W4, so that the overflow F1 containing foreign matter such as oil having a small specific gravity overflows from the overflow port 2264 while swirling. Thus, the water near the water surface in the centrifugal separation chamber 221 is discharged to the drainage channel 224 provided outside the both side walls in the Y direction of the water purification tank 22. On the other hand, the underflow F2 containing foreign matter having a large specific gravity is released from the underflow port 2261 into the water in the centrifugal separation chamber 221. However, the foreign matter having a large specific gravity is deposited on the bottom surface of the centrifugal separation chamber 221, so Clean water sterilized and deodorized with ozone gas A remains in the upper part.

また、荒目フィルタ225Aの上流側の面(上流面)にも、オゾンガスAを含む気泡群を巻き込んだ高圧のジェット水流W4がエジェクタノズル233から噴射されるため、図2(B)に示すように、遠心分離室221内の水が、高圧のジェット水流W4によって荒目フィルタ225Aを介して下流側の濾過室222へ強制的に送り込まれる。これにより、濾過室222には、荒目フィルタ225Aにより処理され、かつ、オゾンガスAで殺菌・脱臭等されたより清浄な水が蓄えられる。また、遠心分離室221内の水の濾過によって荒目フィルタ225Aの上流面に残留した異物のケーキ30が、キャビテーションによって粉砕・除去される。   Further, since a high-pressure jet water flow W4 including a group of bubbles containing ozone gas A is also ejected from the ejector nozzle 233 to the upstream surface (upstream surface) of the coarse filter 225A, as shown in FIG. In addition, the water in the centrifugal separation chamber 221 is forcibly sent to the downstream filtration chamber 222 through the coarse filter 225A by the high-pressure jet water flow W4. As a result, cleaner water treated by the coarse filter 225 </ b> A and sterilized / deodorized with the ozone gas A is stored in the filtration chamber 222. Further, the foreign substance cake 30 remaining on the upstream surface of the coarse filter 225A by the filtration of water in the centrifugal separation chamber 221 is pulverized and removed by cavitation.

同様に、細目フィルタ225Bの上流側の面(上流面)にも、オゾンガスAを含む気泡群を巻き込んだ高圧のジェット水流W4がエジェクタノズル233から噴射されるため、図2(B)に示すように、濾過室222内の水が、高圧のジェット水流W4によって、細目フィルタ225Bを介して下流側の貯水室223に強制的に送り込まれる。これにより、貯水室223には、細目フィルタ225Bにより濾過され、かつ、オゾンガスAで殺菌・脱脱臭等されたより清浄な水が蓄えられる。また、濾過室222内の水の濾過により細目フィルタ225Bの上流面に残留した異物のケーキ30が、キャビテーションによって粉砕・除去される。   Similarly, since the high-pressure jet water flow W4 including the bubbles including the ozone gas A is jetted from the ejector nozzle 233 to the upstream surface (upstream surface) of the fine filter 225B, as shown in FIG. In addition, the water in the filtration chamber 222 is forcibly sent to the downstream water storage chamber 223 via the fine filter 225B by the high-pressure jet water flow W4. Thereby, in the water storage chamber 223, cleaner water filtered by the fine filter 225B and sterilized and deodorized by the ozone gas A is stored. Further, the foreign substance cake 30 remaining on the upstream surface of the fine filter 225B due to the filtration of water in the filtration chamber 222 is pulverized and removed by cavitation.

以上述べたように、本実施の形態によれば、一次濾過水W2とは別途、オゾンガスAの気泡群を含む高圧のジェット水流W4を液体サイクロン226の内部に噴射するため、一次濾過水W2を液体サイクロン226内に高圧で送り込まなくても、液体サイクロン226内部の旋回流の速度を確保することができる。したがって、異物を含む原水を高圧で噴射可能な高性能のポンプを設ける必要がなく、その分、製造コストを低減できる。   As described above, according to the present embodiment, since the high-pressure jet water flow W4 including the bubbles of the ozone gas A is injected into the liquid cyclone 226 separately from the primary filtered water W2, the primary filtered water W2 is used. Even if the liquid cyclone 226 is not fed at a high pressure, the speed of the swirl flow inside the liquid cyclone 226 can be ensured. Therefore, it is not necessary to provide a high-performance pump capable of injecting raw water containing foreign substances at a high pressure, and the manufacturing cost can be reduced correspondingly.

また、オゾンガスAを含む気泡群を巻き込んだ高圧のジェット水流W4がフィルタ225A、225Bの上流面に向けて噴射されるため、浄水運転中、フィルタ225A、225Bの上流面に残留した異物のケーキ30がキャビテーションによって絶えず粉砕・除去される(図2(B)参照)。したがって、フィルタ225A、225Bにケーキ30が固着しないため、フィルタ225A、225Bの逆洗浄を実施しなくても、フィルタ225A、225Bの濾過能力の低下を防止することができる。このため、より長時間にわたる連続浄水運転が可能となる。   In addition, since the high-pressure jet water stream W4 including the bubbles including the ozone gas A is jetted toward the upstream surface of the filters 225A and 225B, the foreign substance cake 30 remaining on the upstream surface of the filters 225A and 225B during the water purification operation. Is constantly pulverized and removed by cavitation (see FIG. 2B). Therefore, since the cake 30 does not adhere to the filters 225A and 225B, it is possible to prevent the filtering ability of the filters 225A and 225B from being lowered even if the filters 225A and 225B are not back-washed. For this reason, continuous water purification operation over a longer time is possible.

また、高圧のジェット水流W4によって濾過対象の水がフィルタ225A、225Bに圧入されるため、濾過速度を向上させることができる。   Further, since the water to be filtered is press-fitted into the filters 225A and 225B by the high-pressure jet water flow W4, the filtration speed can be improved.

さらに、浄水槽22内の各室221〜223に噴射されるジェット水流W4の気泡群にはオゾンガスAが含まれているため、最終的に、よりクリーンな濾過水W5を生成することができる。   Furthermore, since ozone gas A is contained in the bubble group of the jet water flow W4 injected into the chambers 221 to 223 in the water purification tank 22, it is possible to finally generate cleaner filtered water W5.

1:前処理ユニット、2:高水圧浄水ユニット、11:ウエッジスクリーン除塵装置、21:低圧ポンプ、22:浄水槽、23:ジェット水流噴射装置、111:貯水タンク、112:ウエッジスクリーン、113:SS収集タンク、221:遠心分離室、222:濾過室、223:貯水室、224:排水路、225A:荒目フィルタ、225B:細目フィルタ、226:液体サイクロン、231:オゾン発生器、232:高圧ポンプ、233:エジェクタノズル、2261:アンダーフロー口、2262:一次濾過水供給口、2263:ジェット水流供給口、2264:オーバーフロー口 1: Pretreatment unit, 2: High water pressure water purification unit, 11: Wedge screen dust removal device, 21: Low pressure pump, 22: Water purification tank, 23: Jet water jetting device, 111: Water storage tank, 112: Wedge screen, 113: SS Collection tank, 221: centrifuge chamber, 222: filtration chamber, 223: reservoir, 224: drainage channel, 225A: coarse filter, 225B: fine filter, 226: hydrocyclone, 231: ozone generator, 232: high pressure pump 233: Ejector nozzle, 2261: Underflow port, 2262: Primary filtered water supply port, 2263: Jet water flow supply port, 2264: Overflow port

Claims (2)

処理対象水から異物を除去する高水圧浄水装置であって、
原水供給口及び高圧水流供給口を有する液体サイクロンを収容し、当該液体サイクロンの下端開口部からのアンダーフローを貯水する浄水槽と、
前記浄水槽から溢れ出る、前記液体サイクロンの上端開口部からのオーバーフローが流入する排水路と、
前記処理対象水を前記原水供給口から前記液体サイクロンの内部に供給する処理対象供給手段と、
前記高圧水流供給口に取り付けられた第一のエジェクタノズルを有し、オゾンガスを含む気泡を巻き込んだ水流を、前記第一のエジェクタノズルから、前記液体サイクロンの内部に、前記液体サイクロンの内周方向に、前記処理対象水よりも高圧で噴射するジェット水流噴射手段と、を有する
ことを特徴とする高水圧浄水装置。
It is a high water pressure water purification device that removes foreign substances from the water to be treated,
A water purification tank that contains a liquid cyclone having a raw water supply port and a high-pressure water flow supply port, and stores underflow from the lower end opening of the liquid cyclone,
A drainage channel overflowing from the water purification tank, into which overflow from the upper end opening of the hydrocyclone flows;
Processing target supply means for supplying the processing target water from the raw water supply port to the inside of the hydrocyclone;
A first ejector nozzle attached to the high-pressure water flow supply port, and a water flow including bubbles containing ozone gas is introduced from the first ejector nozzle into the liquid cyclone in the inner circumferential direction of the liquid cyclone. And a jet water jet means for jetting at a higher pressure than the water to be treated.
請求項1記載の高水圧浄水装置であって、
前記浄水槽の内部を、前記液体サイクロンを含む第一の室と前記液体サイクロンを含まない第二の室とに仕切るフィルタをさらに有し、
前記ジェット水流噴射手段は、
前記フィルタを介して前記第二の室側に向けられた第二のエジェクタノズルをさらに有し、オゾンガスを含む気泡を巻き込んだ水流を、さらに、前記第二のエジェクタノズルから前記フィルタに向けて噴射する
ことを特徴とする高水圧浄水装置。
The high water pressure water purification device according to claim 1,
A filter that partitions the interior of the water purification tank into a first chamber containing the liquid cyclone and a second chamber not containing the liquid cyclone;
The jet water flow injection means
A second ejector nozzle directed to the second chamber side through the filter is further provided, and a water flow including bubbles containing ozone gas is further injected from the second ejector nozzle toward the filter. A high water pressure water purifier characterized by
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