JP4324784B2 - Dust removal device for separating foreign materials - Google Patents
Dust removal device for separating foreign materials Download PDFInfo
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Description
この発明は、原水中に浮遊物を含有する大量の原水をサイクロンを利用して分離する固液分離装置に関し、特に、下水等の雨水ポンプ場のポンプ吸水槽等を洗浄する洗浄水として、その水槽内の水を浄化して使用する夾雑物分離用除塵装置に関する。 The present invention relates to a solid-liquid separation device that separates a large amount of raw water containing floating substances in raw water using a cyclone, and in particular, as washing water for washing a pump water absorption tank of a rainwater pump station such as sewage. The present invention relates to a dust separation device for separating impurities that purifies and uses water in a water tank.
従来、下水管や河川から雨水ポンプ場に取水する前段の流入渠設備に、沈砂分離機やし渣分離装置を設置して固液分離を行なう処理施設は、例えば、特許文献1に記載してあるように公知である。
また、産業機械の金属またはセラミックなどの加工時に使用した油性あるいは水溶性の加工液を、切削屑から分離するサイクロン型ろ過装置も、例えば、特許文献2に記載してあるように公知である。
Conventionally, a treatment facility that performs solid-liquid separation by installing a sand settling separator or a residue separator in an inflow dredge facility that takes water from a sewage pipe or river to a rainwater pumping station is described in, for example, Patent Document 1 As is known.
A cyclone type filtration device that separates oily or water-soluble processing fluid used during processing of metal or ceramic of industrial machinery from cutting waste is also known as described in Patent Document 2, for example.
上記流入渠設備で使用する沈砂分離機やし渣分離装置では、設置スペースが多く必要で、既設のポンプ場に設置することが難しい。また、分離装置の設置部分で開水路となり、送水及び加圧用ポンプが別途必要となる。この取水した吸水槽等の雨水や下水には、砂、泥分などの沈砂と水に浮ぶ紐、布などのし渣が含まれる。この取水した水を直接使用すると、次工程のポンプ吸水槽等を洗浄する噴射用ノズルに有害な影響を及ぼす。また、従来のクーラント洗浄用サイクロンでは、下水道に適用するにはフイルタが大量のし渣に対応できない。
この発明は、サイクロンを利用して、比重の重い沈砂と比重の軽いし渣が混在する下水等を浄化して、ポンプ吸水槽等の洗浄水として使用できる夾雑物分離用除塵装置を提供する。
The sand settling machine and the screen residue separator used in the above inflow dredge equipment require a lot of installation space and are difficult to install in an existing pumping station. Moreover, it becomes an open channel in the installation part of a separation apparatus, and a pump for water supply and pressurization is needed separately. The rainwater and sewage from the water absorption tank or the like that has taken in water includes sand, mud, and other sediments, and strings such as strings and cloth floating on the water. If this taken water is used directly, it will have a detrimental effect on the spray nozzle that cleans the pump water tank etc. in the next process. In addition, the conventional cyclone for cleaning a coolant cannot handle a large amount of residue when applied to a sewer.
The present invention provides a dust removing device for separating contaminants that can be used as cleaning water for a pump water tank, etc., by using a cyclone to purify sewage and the like in which sand with high specific gravity and light specific gravity are mixed.
この発明に係る夾雑物分離用除塵装置は、密閉円筒槽の周壁に原水の供給管を接線方向に配設し、その槽底を円錐状に形成して沈砂の排出管を連結し、上部に分離液の取出管を設けた夾雑物の分離装置において、中央部に開口を有する仕切壁で密閉円筒槽を第一分離室と第二分離室に区画し、開口に漏斗状のオーバーフローノズルを配設して、第一分離室を構成する密閉円筒槽の周壁に供給管と槽底にアンダーフローノズルを配設すると共に、第二分離室に密閉円筒槽と同心状にスクリーンを配設して、回転自在なスクレーパを円弧状に形成してスクリーンに傾斜させて摺設させ、スクリーンの外側に分離水室を形成し、この分離水室に取出管を連結し、第二分離室を構成する密閉円筒槽の頂壁に連結した排水管に降下管を接続し、降下管を垂下させて逆U字状のサイホン管を構成したもので、第一分離室に接線方向に圧入した原水は、比重の重い砂、泥分の沈砂を遠心力の作用により壁面に沿って旋回させながら沈殿させて分離する。第一分離室の周壁の近傍を旋回する比重の大きい沈砂はオーバーフローノズルの仕切壁に遮られ、第二分離室に流入することがない。そして、旋回しながら第一分離室の中心部に集められたし渣は、分離水の排出によりオーバーフローノズルの縮開された下端から流入し、第二分離室に上昇する。比重の軽いし渣は水とともに第二分離室に流入し、スクリーンに捕捉させる。スクリーンで捕捉した異物は、斜めに取付けたスクレーパのネジ作用で掻取って、異物を頂壁に押上げて目詰まりを防止させることができる。次工程のポンプ吸水槽等を洗浄する噴射用ノズルに有害な夾雑物を取り除くことができる。密閉円筒槽の頂壁に積層させて、分離水とし渣に分離することができる。スクレーパで掻き取られて密閉円筒槽の頂壁に浮上したし渣は、密閉円筒槽の内圧により排水管に押し出され、降下管の負の圧力が作用して排水の流速を早め、し渣の抜出しが容易となる。沈殿した沈砂は、密閉円筒槽の槽底の排出管を状況に応じて開放すれば、密閉円筒槽の内圧により押し出すことができる。 In the dust removing apparatus for separating foreign substances according to the present invention, a raw water supply pipe is disposed in a tangential direction on the peripheral wall of a sealed cylindrical tank, and the tank bottom is formed in a conical shape and connected with a sedimentation discharge pipe. In an apparatus for separating contaminants provided with a separation liquid take-out pipe, a sealed cylindrical tank is divided into a first separation chamber and a second separation chamber by a partition wall having an opening in the center , and a funnel-shaped overflow nozzle is arranged in the opening. A supply pipe and an underflow nozzle are provided on the peripheral wall of the sealed cylindrical tank constituting the first separation chamber, and a screen is provided concentrically with the sealed cylindrical tank in the second separation chamber. A rotatable scraper is formed in an arc shape and is inclined and slid on the screen, a separation water chamber is formed outside the screen, and a take-out pipe is connected to the separation water chamber to constitute a second separation chamber. connect the downcomer to drain which is connected to the top wall of the sealed cylindrical tank, the downcomer Please not be obtained by constituting the inverted U-shaped siphon pipe, the raw water was injected tangentially into the first separation chamber, swirling along the wall surface by the action heavy sand specific gravity, mud fraction of grit of the centrifugal force While precipitating, separate. Sand with a large specific gravity swirling in the vicinity of the peripheral wall of the first separation chamber is blocked by the partition wall of the overflow nozzle and does not flow into the second separation chamber. The residue collected in the center of the first separation chamber while swirling flows in from the lower end of the overflow nozzle contracted by the discharge of the separation water, and rises to the second separation chamber. It lighter specific gravity residue flows into the second separating chamber with water, Ru is trapped in the screen. The foreign matter captured by the screen can be scraped off by the screw action of the scraper attached obliquely, and the foreign matter can be pushed up to the top wall to prevent clogging. It is possible to remove contaminants harmful to the nozzle for injection that cleans the pump water tank or the like in the next step. It can be laminated on the top wall of a sealed cylindrical tank to separate it into separated water as residue. The residue that has been scraped off by the scraper and floated on the top wall of the sealed cylindrical tank is pushed out to the drain pipe by the internal pressure of the sealed cylindrical tank, and the negative pressure of the downcomer acts to increase the flow rate of the drainage. Extraction is easy. The precipitated precipitated sand, the discharge pipe of the tank bottom of a closed cylindrical tank if opened depending on the situation, can be pushed out by the internal pressure of the closed cylindrical tank.
また、スクレーパの回動手段が、スクレーパに連結した主軸を密閉円筒槽の頂壁から突設し、この主軸に水平状の従動軸と、従動軸に垂直状の駆動軸をベベルギヤーを介してそれぞれ連結して、密閉円筒槽の周壁近傍からスクレーパの操作を行うもので、スクリーンの目詰まりの状況に応じて、手動でスクリーン面にスクレーパを摺設させることができる。 The scraper turning means has a main shaft connected to the scraper protruding from the top wall of the sealed cylindrical tank, and a horizontal driven shaft and a drive shaft perpendicular to the driven shaft are connected to the main shaft via bevel gears, respectively. The scraper is operated from the vicinity of the peripheral wall of the sealed cylindrical tank by being connected, and the scraper can be manually slid on the screen surface according to the state of clogging of the screen.
この発明の夾雑物分離用除塵装置は上記のように構成してあり、サイクロンを形成する第一分離室の上段に、円筒状のスクリーンを張設した第二分離室を設置したので、第二分離室のスクリーンで除去するものは比重の軽いものだけでよく、目詰まりを防止するスクレーパの掻取も容易となる。スクリーンは様々な比重の物が混在すると逆洗装置を必要とするが、この発明では、比重の異なる夾雑物の混在が少ないため、逆洗装置を設ける必要がない。そして、沈殿した沈砂と、浮上したし渣の排水工程は、夾雑物分離用除塵装置の運転中でも可能となる。また、密閉構造なので、残圧が利用できるため、分離水の送水用または圧送用のポンプを必要としない。除塵装置がコンパクトなため、設置スペースが少なくて済む。 The dust removing device for separating foreign substances according to the present invention is configured as described above, and the second separation chamber having a cylindrical screen is installed on the upper stage of the first separation chamber forming the cyclone. What is removed by the screen of the separation chamber only needs to be light in specific gravity, and scraper scraping to prevent clogging is easy. The screen requires a backwashing device when various specific gravity objects are mixed, but in the present invention, since there is little mixture of foreign substances having different specific gravity, it is not necessary to provide a backwashing device. The draining process of the settled sand and the levitated residue is possible even during operation of the dust removing apparatus for separating foreign substances. Moreover, since the residual pressure can be used because of the sealed structure, a pump for feeding separated water or pumping is not required. Since the dust removal device is compact, it requires less installation space.
この発明に係る夾雑物分離用除塵装置を図面に基づき詳述すると、図1は密閉円筒槽の要部縦断面図であって、密閉円筒槽1は槽底1aを円錐状に形成し、中央部に開口2aを有する仕切壁2を水平状に配設してある。この仕切壁2の開口2aに漏斗状のオーバーフローノズル3の上端を支架してあり、密閉円筒槽1を下方の第一分離室4と上方の第二分離室5に区画する。第一分離室4の密閉円筒槽1の周壁1bに原水の供給管6が接線方向に連結してあり、原水を第一分離室4に圧入し、オーバーフローノズル3の下面周部に旋回しながら流入させる。第一分離室4に流入した比重の重い砂、泥分の沈砂は、遠心作用により壁面に沿って旋回し、仕切壁2とオーバーフローノズル3の下面周壁に遮られ、減速しながら沈殿し、円錐状の槽底1aの傾斜面を滑り落ちて中央部に集積される。沈砂を分離した比重の軽いし渣は、旋回しながら第一分離室4の中心部に集められ、漏斗状のオーバーフローノズル3の下端から水とともに第二分離室5に流入する。 Referring to the drawings, the dust removing apparatus for separating impurities according to the present invention will be described in detail. FIG. 1 is a longitudinal sectional view of a main part of a sealed cylindrical tank. A partition wall 2 having an opening 2a in the part is arranged horizontally. An upper end of a funnel-shaped overflow nozzle 3 is supported on the opening 2a of the partition wall 2, and the sealed cylindrical tank 1 is divided into a lower first separation chamber 4 and an upper second separation chamber 5. A raw water supply pipe 6 is tangentially connected to the peripheral wall 1 b of the sealed cylindrical tank 1 of the first separation chamber 4, and the raw water is press-fitted into the first separation chamber 4 and swirling around the lower surface of the overflow nozzle 3. Let it flow. Sand with a high specific gravity and mud sediment flowing into the first separation chamber 4 is swung along the wall surface by centrifugal action, blocked by the lower wall of the partition wall 2 and the overflow nozzle 3, and settled while decelerating. The bottom of the tank-shaped tank bottom 1a slides down and accumulates in the center. Sediment having a low specific gravity after separating the settling sand is collected in the center of the first separation chamber 4 while swirling, and flows into the second separation chamber 5 together with water from the lower end of the funnel-shaped overflow nozzle 3.
密閉円筒槽1の槽底1aの中央部にアンダーフローノズル7が配設してあり、アンダーフローノズル7に沈砂の排出管8を連結して、排出管8にボール弁9を介装してある。第一分離室4の底部に集積された沈殿物は、ボール弁9を開放すれば、密閉円筒槽1のヘッド圧とアンダーフローノズル7の抽水作用により、排水の流速を促進させ、排出管8から沈殿した沈砂を排出する。
沈殿した夾雑物の排水工程は、夾雑物分離用除塵装置の運転中でも可能である。
Underflow nozzle 7 in the central portion of the closed cylindrical tank 1 the tank bottom 1a is Yes and arranged, by connecting the emissions tube 8 of the sand in the underflow nozzle 7, interposed a
The drainage process of the precipitated contaminants can be performed even during operation of the dust separator for separating contaminants.
図1に示すように、第二分離室5に密閉円筒槽1と同心状にスクリーン10が配設してあり、密閉円筒槽1とスクリーン10の間に分離水室11が形成してある。第二分離室5の周部に張設したスクリーン10の目開きは、10〜20mmとしてある。次工程のポンプ吸水槽等を洗浄する噴射用ノズルに有害な夾雑物だけを取り除くようにしてある。水とともに第二分離室5に流入した比重の軽いし渣は、スクリーン10に捕捉され、し渣を分離した水は分離水室11に流入する。分離水室11の周壁の密閉円筒槽1に取出管12が連結してあり、し渣を分離した分離水は密閉円筒槽1の内圧で抜出される。密閉構造の密閉円筒槽1は、残圧が利用できるため、分離水の送水用または圧送用のポンプを必要としない。次工程の噴射用ノズルに夾雑物を取り除いた洗浄水を送水することができる。 As shown in FIG. 1, a screen 10 is disposed concentrically with the sealed cylindrical tank 1 in the second separation chamber 5, and a separation water chamber 11 is formed between the sealed cylindrical tank 1 and the screen 10. The opening of the screen 10 stretched around the periphery of the second separation chamber 5 is 10 to 20 mm. Only the contaminants harmful to the nozzle for spraying which cleans the pump water tank etc. in the next process are removed. The scum of light specific gravity that flows into the second separation chamber 5 together with the water is captured by the screen 10, and the water from which the slag has been separated flows into the separation water chamber 11. An extraction pipe 12 is connected to the sealed cylindrical tank 1 on the peripheral wall of the separation water chamber 11, and the separated water from which the residue has been separated is drawn out by the internal pressure of the sealed cylindrical tank 1. Since the sealed cylindrical tank 1 having a sealed structure can use the residual pressure, it does not require a pump for feeding separated water or for feeding pressure. Wash water from which impurities have been removed can be sent to the nozzle for injection in the next step.
図2は、密閉円筒槽の上部の縦断面図であって、密閉円筒槽1の頂壁1cの中央部にパッキンを収納したパッキン箱13が配設してあり、このパッキン箱13に軸支された主軸14が第二分離室5に垂下してある。主軸14の下端に水平状に配設した支持杆15に、一対の円弧状のスクレーパ16、16が傾斜させて止着してある。このスクレーパ16のスクレーパエッジ16aをスクリーン10に摺設させてある。図1に示すように、スクレーパ16の主軸14の上端部が密閉円筒槽1の頂壁1cから突設してあり、この主軸14にベベルギヤー17、17を介して従動軸18を水平状に連結し、更に、この従動軸18にベベルギヤー19、19を介して垂設した駆動軸20に連結してある。駆動軸20の下端にハンドル21が止着してあり、必要に応じて密閉円筒槽1の周壁1b近傍からスクレーパ16を操作ができるようにしてある。
FIG. 2 is a vertical cross-sectional view of the upper part of the sealed cylindrical tank, and a
図2に示すように、スクリーン10で捕捉した異物は、スクリーン10に斜めに摺接させるスクレーパ16のネジ作用で掻取られ、し渣を密閉円筒槽1の頂壁1cに押上げて目詰まりを防止させる。第二分離室5のスクリーン10で除去するものは比重の軽いものだけでよく、目詰まりを防止するスクレーパ16の掻取も容易となる。スクリーン10は様々な比重の物が混在すると逆洗装置を必要とするが、この発明では、比重の異なる夾雑物の混在が少ないため、逆洗装置を設ける必要がない。なお、図示を省略するが、手動の代わりに主軸14の上端部に駆動機を連動連結して、電動でスクレーパ16を回動させてもよいものである。図3は密閉円筒槽の平面図であって、密閉円筒槽の頂壁1cに点検窓22が配設してあり、第二分離室5の内部が見えるようにしてあり、スクリーン10の目詰まり状況が把握できるものである。
As shown in FIG. 2, the foreign matter captured by the screen 10 is scraped by the screw action of the scraper 16 slidably contacting the screen 10, and the residue is pushed up to the top wall 1 c of the sealed cylindrical tank 1 and clogged. To prevent. The screen 10 of the second separation chamber 5 only needs to be removed with a light specific gravity, and the scraper 16 that prevents clogging can be easily scraped off. The screen 10 needs a backwashing device when various specific gravity objects are mixed, but in the present invention, since there is little mixture of foreign substances having different specific gravity, it is not necessary to provide a backwashing device. In addition, although illustration is abbreviate | omitted, a scraper 16 may be rotated electrically by interlockingly connecting a drive machine with the upper end part of the main shaft 14 instead of manual operation. FIG. 3 is a plan view of the sealed cylindrical tank, in which an
図1に示すように、密閉円筒槽1の頂壁1cに排水管23が連結してあり、排水管23に連結した降下管24を密閉円筒槽1の下方に垂下させてサイホン管25を構成してある。降下管24の下端部に開閉弁26が介装してあり、開閉弁26を開放すれば、第二分離室5の上方に浮上したし渣は、密閉円筒槽1の内圧により排水管23に押し出すことができる。排水管23に連結した降下管24はサイホン作用による負の圧力が作用して排水の流速を早め、し渣の抜出しが容易となる。浮上したし渣の排水工程は、夾雑物分離用除塵装置の運転中でも可能となる。
As shown in FIG. 1, a drain pipe 23 is connected to the top wall 1 c of the sealed cylindrical tank 1, and a downcomer 24 connected to the drain pipe 23 is suspended below the sealed cylindrical tank 1 to form a siphon pipe 25. It is. An opening / closing
この発明に係る夾雑物分離用除塵装置は、密閉円筒槽にサイクロンを形成して、比重の重い夾雑物を分離する第一分離室と、その上段に比重の軽いし渣などを分離する第二分離室を設置したので、第二分離室のスクリーンで除去するものは比重の軽いものだけでよく、目詰まりを防止するスクレーパの掻取も容易となる。したがって、下水等の雨水ポンプ場や浄水場の水槽内の原水から夾雑物の分離が可能となり、大量の洗浄水を必要とするポンプ吸水槽等とその設備機器に洗浄水を供給する大型の夾雑物分離用除塵装置として利用できる。 The dust separating apparatus for separating impurities according to the present invention forms a cyclone in a sealed cylindrical tank, and separates a dust having a high specific gravity in a first separation chamber that separates heavy impurities and a second portion that separates a light residue, etc. Since the separation chamber is installed, only the lighter specific gravity needs to be removed by the screen of the second separation chamber, and scraper scraping to prevent clogging is easy. Therefore, it becomes possible to separate impurities from the raw water in rainwater pumping stations such as sewage and water purification plants, and large contaminants that supply cleaning water to pump water tanks and other equipment that require large amounts of cleaning water. It can be used as a dust removal device for separating objects.
1 密閉円筒槽
1a 槽底
1b 周壁
1c 頂壁
2 仕切壁
2a 開口
3 オーバーフローノズル
4 第一分離室
5 第二分離室
6 供給管
7 アンダーフローノズル
8 排出管
10 スクリーン
11 分離水室
12 取出管
14 主軸
16 スクレーパ
17、19 ベベルギヤー
18 従動軸
20 駆動軸
23 排水管
24 降下管
25 サイホン管
DESCRIPTION OF SYMBOLS 1 Sealed cylindrical tank 1a Tank bottom 1b Perimeter wall 1c Top wall 2 Partition wall 2a Opening 3 Overflow nozzle 4 First separation chamber
5 Second Separation Chamber 6 Supply Pipe 7 Underflow Nozzle 8 Discharge Pipe 10 Screen 11 Separation Water Chamber 12 Take-out Pipe 14 Spindle 16 Scraper 17, 19 Bevel Gear 18 Driven Shaft 20 Drive Shaft 23 Drain Pipe 24 Downcomer Pipe 25 Siphon Pipe
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KR100725443B1 (en) | 2005-10-13 | 2007-06-07 | 닛코 킨조쿠 가부시키가이샤 | How to treat dust with coins |
CN102642938A (en) * | 2011-02-16 | 2012-08-22 | 江苏长源环保设备有限公司 | High-turbidity tower-shaped water purifier |
CN109459278B (en) * | 2018-11-28 | 2021-10-26 | 北京林业大学 | Accurate sampling device of quality of water layering |
CN109351050A (en) * | 2018-11-30 | 2019-02-19 | 天津大学 | A kind of high-efficiency cyclone separation treatment device for initial rainwater and method thereof |
CN113800713B (en) * | 2021-09-08 | 2024-01-09 | 黑龙江省捷浩建筑工程有限公司 | Domestic sewage treatment device and treatment method |
CN113796295B (en) * | 2021-10-14 | 2022-08-23 | 湖南金蓝田环保工程有限公司 | Environment-friendly water conservancy irrigation device |
CN117990168B (en) * | 2024-02-18 | 2024-07-23 | 江苏宏达仪表科技有限公司 | High-precision flowmeter suitable for chimney flow monitoring |
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