JP2003320372A - Filter for water environment - Google Patents
Filter for water environmentInfo
- Publication number
- JP2003320372A JP2003320372A JP2002166348A JP2002166348A JP2003320372A JP 2003320372 A JP2003320372 A JP 2003320372A JP 2002166348 A JP2002166348 A JP 2002166348A JP 2002166348 A JP2002166348 A JP 2002166348A JP 2003320372 A JP2003320372 A JP 2003320372A
- Authority
- JP
- Japan
- Prior art keywords
- water
- filter
- casing
- mesh screen
- foreign matters
- Prior art date
- Legal status (The legal status is an assumption and is not a legal conclusion. Google has not performed a legal analysis and makes no representation as to the accuracy of the status listed.)
- Pending
Links
- XLYOFNOQVPJJNP-UHFFFAOYSA-N water Substances O XLYOFNOQVPJJNP-UHFFFAOYSA-N 0.000 title claims abstract description 71
- 238000001914 filtration Methods 0.000 claims abstract description 41
- 239000012528 membrane Substances 0.000 claims description 33
- 238000005406 washing Methods 0.000 abstract description 12
- 238000000034 method Methods 0.000 abstract description 8
- 238000007664 blowing Methods 0.000 abstract 1
- 230000007547 defect Effects 0.000 abstract 1
- 238000007599 discharging Methods 0.000 abstract 1
- 238000005507 spraying Methods 0.000 abstract 1
- 238000011001 backwashing Methods 0.000 description 8
- 239000008213 purified water Substances 0.000 description 5
- 239000000356 contaminant Substances 0.000 description 4
- 239000000126 substance Substances 0.000 description 4
- 238000004140 cleaning Methods 0.000 description 2
- 239000000463 material Substances 0.000 description 2
- 238000009287 sand filtration Methods 0.000 description 2
- 239000010865 sewage Substances 0.000 description 2
- 230000003749 cleanliness Effects 0.000 description 1
- 230000007423 decrease Effects 0.000 description 1
- 238000010586 diagram Methods 0.000 description 1
- 230000000694 effects Effects 0.000 description 1
- JEGUKCSWCFPDGT-UHFFFAOYSA-N h2o hydrate Chemical compound O.O JEGUKCSWCFPDGT-UHFFFAOYSA-N 0.000 description 1
- 239000008235 industrial water Substances 0.000 description 1
- 239000010813 municipal solid waste Substances 0.000 description 1
- 230000002250 progressing effect Effects 0.000 description 1
- 125000006850 spacer group Chemical group 0.000 description 1
- 239000007921 spray Substances 0.000 description 1
- 239000002344 surface layer Substances 0.000 description 1
- 238000003911 water pollution Methods 0.000 description 1
Landscapes
- Separation Using Semi-Permeable Membranes (AREA)
Abstract
Description
【発明の詳細な説明】
【0001】
【発明の属する技術分野】産業上に於いて使用される上
水又は下水又は一般生活用上、下、水の場に於いて用い
られる水の利用過程に於ける重要な作業として水中に混
在するごみ等水以外の介雑物を除去する作業は一般にフ
ィルターなどに水を通過させることによって行われてい
る。清浄な水を求める場合はフィルターのメッシュの大
きさを縮小することに比例して清浄度も良くなるがフィ
ルターに蓄積される雑介物によってフィルターを通過す
る水量が制御され通過水量と雑介物の単位あたり混在量
とは反比例の関係で供給水量に影響を及ぼす結果となる
為にフィルターは常に一定の浄化力と通過水量を確保す
ることが要求される。したがって、フィルター面の通過
入水側の表面を清浄にする目的で経路流水を逆流洗浄す
る考え方等により様々なシステムが実施されている。
【0002】
【発明の解決しようとする課題】汚染した水質を効率的
に浄化する手法について水質汚染が急激に進行する近代
に於いては重要課題であり単位あたりの水量を膜によっ
て浄化するためのコストを限りなく低くする事が望まれ
ている。本考案によるフィルター膜面の洗浄技術に類似
するシステムは存在するが装置の構造上及び採用素材等
の理由により小型で一般に広く採用されるには至ってい
ない。この問題を解決する目的で小容量から大容量に対
応すると共に省力的なフィルターを提供しようとするも
のである。現在一般に用いられている濾過装置を大別す
ると砂濾過と膜又はスリット等によりメッシュ又はスリ
ットの開口部に水を通過させる手法がある。砂濾過の場
合は濾過精度にばらつきがあり膜式に対して装置の大型
化が要求される。今後の濾過装置の理想は装置の単位能
力容積が小さく濾過精度を規定する事が出来る事が望ま
れる。
【0003】
【課題を解決するための手段】膜式又はスリットタイプ
の濾過装置はこれからのフィルターとしての理想を充足
するが入水側の膜面又はスリット面に水中より濾過分離
された雑介物によって濾過膜面又はスリット入水面が閉
塞状態となる為に濾過膜面を常に清浄に保つ必要から逆
洗浄の手法により膜面のリフレッシュを行う必要がある
が膜面に積層した雑介物は逆洗による反対流のみでは膜
面からの離脱が容易に出来ない。本考案では逆洗状態を
保ちながら入水側に高圧配管を設置して濾過膜の入水側
フィルター膜面を回転移動して洗浄する為のノズルを高
圧配管上に並列して取りつけて清浄水によって入水側濾
過膜面を洗浄する事によって逆洗流と共に膜面より剥離
した雑介物は逆洗時に同時に解放されたドレン排水口よ
り濾過装置外に排出される。
【0004】
【発明の実施の形態】本発明の代表的な事例を
【図1】
【図2】により説明する。
【図1】は請求項1による濾過装置の構造と機能を説明
する為の
【図2】A−A’の破線で切った濾過装置の横方向から
みた断面図である。本濾過装置の濾過プロセスを説明す
る。濾過を必要とする水はポンプ17を介して一定の圧
力により濾過装置(以後装置R、とする)底部に開口す
るパイプ1より装置Rに流入することにより濾過膜10
の全面より濾過された水は装置Rのケーシング12と濾
過膜10との空間16に析出し清浄水となって濾過処理
水出口2より排出する。一定の濾過が経過すると濾過膜
内面に入水中の雑介物が析出付着して濾過膜を通過する
浄化水量が減少すると共に入水側1の圧力と出水側2の
圧力に差が生ずることを利用して制御装置25を作動さ
せてバルブ20及び22を閉じると共にバルブ21及び
23を開放し同時にポンプ17を停止しラインポンプ1
8をONとして浄化水槽24から送水される浄化水はケ
ーシング12内のスペース16を介して濾過膜の逆洗を
行うと同時に浄化水槽24から高圧ポンプ19によって
高圧水管5に高圧水を供給すると共に高圧水管5回転動
力8によって高圧水管5は装置Rの中心部で回転しなが
ら加圧水吐出口11から逆洗中の濾過膜10の表層に付
着した雑介物を噴射洗浄し落下雑介物は逆洗浄水と共に
バルブ21によって開放されたドレン開口部4から排出
される事となる。濾過膜の洗浄時間は洗浄状況を人為的
判断基準の時間による自動制御とラインポンプ18の圧
力変化によって作動制御する自動システムが考えられ
る。流入水の濾過を継続的に行う場合は装置12を複数
設置する必要がある。本発明による濾過装置は濾過膜面
を流速差を利用して相対する強さの異なる水流を濾過膜
面に作動させる事によって強く付着する雑介物を効率良
く完全に除去する事と共に濾過装置の単位容量当たりに
必要とするシステム全体の規模をより小さくする事が出
来る。また濾過膜のメッシュを必要とするレベルで自由
に選択する事が可能となる。Description: BACKGROUND OF THE INVENTION The present invention relates to a process of utilizing water used in industrial water, sewage or general living, sewage and water. As an important work in the art, the work of removing contaminants other than water such as trash mixed in water is generally performed by passing water through a filter or the like. When purifying clean water, the cleanliness improves in proportion to the size of the filter mesh, but the amount of water passing through the filter is controlled by the miscellaneous matter accumulated in the filter, and the amount of water passing through and the miscellaneous matter The filter is required to always maintain a constant purifying power and a constant flow rate of water in order to have an effect on the amount of supplied water in an inversely proportional relationship with the mixed amount per unit. Therefore, various systems have been implemented based on the concept of backwashing the flowing water in order to clean the surface of the filter surface on the passing water inlet side. [0002] A method for efficiently purifying polluted water quality is an important issue in modern times when water pollution is rapidly progressing, and is a method for purifying water quantity per unit by a membrane. It is desirable to keep costs as low as possible. Although a system similar to the filter membrane cleaning technique according to the present invention exists, it is small and has not been widely adopted because of the structure of the apparatus and the material used. An object of the present invention is to provide a filter that can handle a small capacity to a large capacity and that can save labor. A filtering device generally used at present is roughly classified into a method of passing water through an opening of a mesh or a slit by sand filtration and a membrane or a slit. In the case of sand filtration, the filtration accuracy varies and a larger apparatus is required for a membrane type. In the future, it is desired that the filtering device has a small unit capacity of the device and can regulate the filtering accuracy. [0003] A membrane or slit type filtration device satisfies the ideal as a filter in the future, but is provided with a contaminant filtered and separated from the water on the membrane surface or slit surface on the water inlet side. Since the filter membrane surface or slit water inlet surface is blocked, it is necessary to keep the filter membrane surface clean at all times, so it is necessary to refresh the membrane surface by a backwashing method, but miscellaneous materials laminated on the membrane surface are backwashed It is not easy to separate from the membrane surface only by the counterflow due to. In the present invention, a high pressure pipe is installed on the water inlet side while maintaining the backwashing state, and a nozzle for rotating and moving the filter membrane surface on the water inlet side of the filtration membrane for cleaning is mounted in parallel on the high pressure pipe and water is supplied with clean water. The contaminants separated from the membrane surface together with the backwashing flow by washing the side filtration membrane surface are discharged to the outside of the filtration device from the drain drain port opened at the same time as the backwashing. [0004] A typical case of the present invention will be described with reference to FIG. 1 and FIG. BRIEF DESCRIPTION OF THE DRAWINGS FIG. 1 is a cross-sectional view of a filtration device taken along a line AA 'and viewed from a lateral direction for explaining the structure and function of the filtration device according to claim 1. The filtration process of the present filtration device will be described. The water that needs to be filtered flows into the filter R from the pipe 1 opening at the bottom of the filter (hereinafter referred to as the device R) through the pump 17 at a constant pressure through the pump 17, whereby the filtration membrane 10 is removed.
The water filtered from the entire surface is deposited in the space 16 between the casing 12 and the filtration membrane 10 of the apparatus R, becomes clean water, and is discharged from the filtered water outlet 2. After a certain amount of filtration, foreign substances in the water are deposited and adhere to the inner surface of the filtration membrane, and the amount of purified water passing through the filtration membrane decreases, and the difference between the pressure on the water inlet side 1 and the pressure on the water outlet side 2 is used. Then, the control device 25 is operated to close the valves 20 and 22 and open the valves 21 and 23, and at the same time, the pump 17 is stopped.
The purified water sent from the purified water tank 24 with 8 turned on performs back washing of the filtration membrane through the space 16 in the casing 12 and simultaneously supplies high-pressure water from the purified water tank 24 to the high-pressure water pipe 5 by the high-pressure pump 19. The high-pressure water pipe 5 is rotated at the center of the apparatus R by the high-pressure water pipe 5 while rotating the high-pressure water pipe 5 to spray and wash miscellaneous substances adhering to the surface layer of the filtration membrane 10 being backwashed from the pressurized water discharge port 11 and reverse the falling miscellaneous substances. The water is discharged from the drain opening 4 opened by the valve 21 together with the washing water. An automatic system in which the washing time of the filtration membrane is controlled automatically by the time of the artificial judgment criterion and the operation control by the pressure change of the line pump 18 can be considered. When filtering the inflow water continuously, it is necessary to install a plurality of devices 12. The filtering device according to the present invention efficiently removes strongly adhered contaminants by operating water flows having different intensities on the filtering membrane surface by utilizing the flow velocity difference, and efficiently removes the foreign substances attached to the filtering membrane surface. The size of the entire system required per unit capacity can be reduced. Also, the mesh of the filtration membrane can be freely selected at a required level.
【図面の簡単な説明】
【図 1】 請求項第1項による水環境用濾過装置の代
表的1例の
【図2】のA−A’の破線の断面による説明図。
【図 2】 請求項第1項による水環境用濾過装置のケ
ーシング中央部を水平面で切った状態の説明の為の切断
図。
【図 3】 本水環境濾過装置を運転するための作業手
順を説明するためのシステムフロー。
【符号の説明】
1.濾過処理前の水の入水口
2.濾過処理水の出口
3.濾過膜洗浄用高圧水入口
4.濾過膜洗浄時に開口するドレン出口
5.動力8によって回転する濾過膜洗浄用高圧水管
6.高圧水管5が回転するための継ぎ手
7.継ぎ手6と高圧水管5のしゅう動部メカニカルシー
ル
8.高圧水管5回転用動力
9.濾過膜固定用スペーサー
10.濾過膜
11.加圧水吐出口
12.筒状ケーシング
13.高圧水管5に取り付けられた傘歯車
14.動8に取り付け歯車13を駆動する傘歯車
15.高圧水管5の底部軸受
16.濾過された水のスペース
17.濾過装置への送水ポンプ
18.逆洗用ラインポンプ
19.高圧ポンプ濾過膜洗浄用
20.流入水バルブ
21.排出用ドレンバルブ
22.清浄水送出バルブ
23.逆洗時逆送水バルブ
24.浄化水槽
25.制御装置
26.レベル制御
27.清浄水送出管BRIEF DESCRIPTION OF THE DRAWINGS FIG. 1 is an explanatory diagram of a representative example of a water environment filtering device according to claim 1 as indicated by a cross-section taken along a line AA ′ in FIG. 2; FIG. 2 is a cutaway view for explaining a state in which a casing central portion of the water environment filtration device according to claim 1 is cut along a horizontal plane. FIG. 3 is a system flow for explaining an operation procedure for operating the present water environment filtration device. [Explanation of Codes] 1. Water inlet before filtration 2. outlet of filtered water 3. High pressure water inlet for filtration membrane washing 4. Drain outlet that opens when washing the filtration membrane 5. High-pressure water pipe for filtration membrane washing rotated by power 8 6. Joint for rotating high-pressure water pipe 5 7. Mechanical seal for sliding part of joint 6 and high-pressure water pipe 5 Power for 5 rotations of high pressure water pipe 9. Spacer for fixing filtration membrane 10. Filtration membrane11. Pressurized water outlet 12. Tubular casing 13. 13. Bevel gear attached to high-pressure water pipe 5. 4. Bevel gears that drive the gears 13 attached to the motion 8. 15. bottom bearing of high-pressure water pipe 5 17. Space for filtered water Water pump to filtration device 18. Backwashing line pump 19. High pressure pump for filtration membrane washing 20. Inflow water valve 21. Drain valve 22. Clean water delivery valve 23. Backwater valve for backwashing 24. Purified water tank 25. Control device 26. Level control 27. Clean water delivery pipe
Claims (1)
シングを鉛直状に設置して中心上部から前記ケーシング
から独立して回転出来る構造をもった加圧水配管を前記
ケーシングの中心軸線状に取りつけ同時に前記ケーシン
グ底部中心に軸受けにより支持し加圧水配管の円周上の
1点の又は複数ヶ所の上下を結ぶ線状に均等の間隔に開
口した加圧水吐出口を設け前記ケーシング内面に添って
凹凸状の面をかたちづくり同時に前記ケーシングの上面
及び下底面にシール状態で取りつけた濾過膜を構成し濾
過膜内の前記ケーシングの底面に処理前水の入り口とド
レン用の出口の開口部を取りつける。又前記濾過膜と前
記ケーシングの側面に開口する構造をもった水環境用濾
過装置。Claims: 1. A pressurized water pipe having a structure in which an independently sealed cylindrical casing is installed vertically and rotatable independently from the casing from above the center, and a central axis of the casing is provided. At the same time, a pressurized water discharge port which is supported by a bearing at the center of the bottom of the casing and is opened at equal intervals in a line connecting one point or a plurality of places on the circumference of the pressurized water pipe is provided along the inner surface of the casing. At the same time, a filtration membrane is formed in a sealed state on the upper and lower bottom surfaces of the casing, and the inlet of the pretreatment water and the drain opening are attached to the bottom surface of the casing in the filtration membrane. . Further, a filtering device for water environment having a structure that is opened on the side surface of the filtration membrane and the casing.
Priority Applications (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
JP2002166348A JP2003320372A (en) | 2002-04-30 | 2002-04-30 | Filter for water environment |
Applications Claiming Priority (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
JP2002166348A JP2003320372A (en) | 2002-04-30 | 2002-04-30 | Filter for water environment |
Publications (1)
Publication Number | Publication Date |
---|---|
JP2003320372A true JP2003320372A (en) | 2003-11-11 |
Family
ID=29545864
Family Applications (1)
Application Number | Title | Priority Date | Filing Date |
---|---|---|---|
JP2002166348A Pending JP2003320372A (en) | 2002-04-30 | 2002-04-30 | Filter for water environment |
Country Status (1)
Country | Link |
---|---|
JP (1) | JP2003320372A (en) |
Cited By (3)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
JP2008272727A (en) * | 2007-05-07 | 2008-11-13 | Saitekkusu Kenkyusho:Kk | Manufacturing method of equipment for decomposing and separating molecule of gas |
CN109574150A (en) * | 2019-01-09 | 2019-04-05 | 广东台泉环保科技有限公司 | A kind of rotating disc type percolate sewage accelerating separtor |
CN110028175A (en) * | 2018-01-12 | 2019-07-19 | 中国石油天然气股份有限公司 | Oil-gas well fracturing flowback fluid treatment method and device and skid-mounted box |
-
2002
- 2002-04-30 JP JP2002166348A patent/JP2003320372A/en active Pending
Cited By (3)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
JP2008272727A (en) * | 2007-05-07 | 2008-11-13 | Saitekkusu Kenkyusho:Kk | Manufacturing method of equipment for decomposing and separating molecule of gas |
CN110028175A (en) * | 2018-01-12 | 2019-07-19 | 中国石油天然气股份有限公司 | Oil-gas well fracturing flowback fluid treatment method and device and skid-mounted box |
CN109574150A (en) * | 2019-01-09 | 2019-04-05 | 广东台泉环保科技有限公司 | A kind of rotating disc type percolate sewage accelerating separtor |
Similar Documents
Publication | Publication Date | Title |
---|---|---|
KR101462631B1 (en) | High flow disc filter | |
JP3903470B2 (en) | Backwash valve | |
KR19990014757A (en) | Apparatus and method for backwashing a fluid filter system | |
HRP20050566A2 (en) | Filter device | |
KR101759931B1 (en) | Light filter type terraced filtering wetland | |
JP4609622B2 (en) | Filtration device | |
KR102527754B1 (en) | First flush rainwater treating apparatus for filter cleaning fucntion | |
KR20170122153A (en) | Rotor filter system with auto-reactivation function | |
CN100438945C (en) | Press filter type water purification method and device thereof | |
CN113943060A (en) | Integrated environment-friendly water purification process for high-rise building | |
JP6544525B2 (en) | Backwashing device moving type filtration device, backwashing device, backwashing method | |
KR100257861B1 (en) | Automatic filter | |
KR20160004499A (en) | Drum Screen Device for Water Purification | |
JP2003320372A (en) | Filter for water environment | |
US20050184011A1 (en) | Car wash water reclamation system | |
KR101985292B1 (en) | Water purification device with filter automatic cleaning function | |
CN102527127B (en) | Sewage filter treatment system | |
KR200420158Y1 (en) | Automatic Precision Filtration Device | |
KR20190081454A (en) | Filter washing type terraced filtering wetland | |
KR20190073858A (en) | Apparatus for cleaning multiple air filter automatically | |
WO2020026275A2 (en) | Automatic backwash filter | |
KR100718547B1 (en) | Rotary Upflow Water Filtration Device | |
KR100424346B1 (en) | Adulteration exclusion device in sewage and wastewater | |
CN114716039B (en) | Materialized treatment wastewater recycling device | |
KR100646309B1 (en) | Rotary multilayer membrane upflow water filtration |