JPH044007A - Filter - Google Patents
FilterInfo
- Publication number
- JPH044007A JPH044007A JP10044490A JP10044490A JPH044007A JP H044007 A JPH044007 A JP H044007A JP 10044490 A JP10044490 A JP 10044490A JP 10044490 A JP10044490 A JP 10044490A JP H044007 A JPH044007 A JP H044007A
- Authority
- JP
- Japan
- Prior art keywords
- filter body
- partition plate
- rotating shaft
- hollow rotating
- filter
- 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
- 239000002245 particle Substances 0.000 claims abstract description 16
- 238000001914 filtration Methods 0.000 claims abstract description 14
- 238000005192 partition Methods 0.000 claims abstract description 11
- 239000000356 contaminant Substances 0.000 claims abstract description 5
- 239000007788 liquid Substances 0.000 claims description 17
- 239000003344 environmental pollutant Substances 0.000 claims description 3
- 231100000719 pollutant Toxicity 0.000 claims description 3
- 239000000725 suspension Substances 0.000 description 11
- 239000010419 fine particle Substances 0.000 description 6
- 239000004576 sand Substances 0.000 description 6
- XLYOFNOQVPJJNP-UHFFFAOYSA-N water Substances O XLYOFNOQVPJJNP-UHFFFAOYSA-N 0.000 description 6
- 238000011001 backwashing Methods 0.000 description 4
- 230000000694 effects Effects 0.000 description 3
- 239000012528 membrane Substances 0.000 description 3
- 238000001223 reverse osmosis Methods 0.000 description 3
- 239000013535 sea water Substances 0.000 description 3
- 229910001220 stainless steel Inorganic materials 0.000 description 3
- 238000011109 contamination Methods 0.000 description 2
- 238000010612 desalination reaction Methods 0.000 description 2
- 238000005516 engineering process Methods 0.000 description 2
- 239000000706 filtrate Substances 0.000 description 2
- 230000005484 gravity Effects 0.000 description 2
- 239000002184 metal Substances 0.000 description 2
- 238000000034 method Methods 0.000 description 2
- 239000010935 stainless steel Substances 0.000 description 2
- RHZUVFJBSILHOK-UHFFFAOYSA-N anthracen-1-ylmethanolate Chemical compound C1=CC=C2C=C3C(C[O-])=CC=CC3=CC2=C1 RHZUVFJBSILHOK-UHFFFAOYSA-N 0.000 description 1
- 239000003830 anthracite Substances 0.000 description 1
- 238000004140 cleaning Methods 0.000 description 1
- 230000001112 coagulating effect Effects 0.000 description 1
- 230000007423 decrease Effects 0.000 description 1
- 230000006866 deterioration Effects 0.000 description 1
- 230000003311 flocculating effect Effects 0.000 description 1
- 239000010410 layer Substances 0.000 description 1
- 244000005700 microbiome Species 0.000 description 1
- 230000000149 penetrating effect Effects 0.000 description 1
- 239000000843 powder Substances 0.000 description 1
- 238000002203 pretreatment Methods 0.000 description 1
- 239000002344 surface layer Substances 0.000 description 1
- 238000005406 washing Methods 0.000 description 1
Abstract
Description
【発明の詳細な説明】
〔産業上の利用分野〕
本発明は、逆浸透膜プロセスの前処理装置等に適用され
るテ過器に関する。DETAILED DESCRIPTION OF THE INVENTION [Field of Industrial Application] The present invention relates to a filter that is applied to a pretreatment device for a reverse osmosis membrane process.
海水より水を製造する逆浸透膜海水淡水化装置において
は、その汚れを除去することがきわめて重要な技術であ
る。海水中には微生物、懸濁物等が浮遊しており、これ
ら浮遊物が後流の淡水化装置に持ち込まれると漠の汚染
、劣化音生じるため、そ几ら全前も理装置で除去する必
要がある。In reverse osmosis membrane seawater desalination equipment that produces water from seawater, removing contamination is an extremely important technology. There are microorganisms, suspended matter, etc. floating in the seawater, and if these suspended matter are brought into the downstream desalination equipment, they will cause vague contamination and deterioration sounds, so all of them must be removed using cleaning equipment. There is a need.
従来、逆浸透膜プロセスの前処理装置として、凝集砂濾
過器が使用されてい念が、次のような問題点があった。Conventionally, coagulating sand filters have been used as pretreatment equipment for reverse osmosis membrane processes, but they have had the following problems.
(1)前処理設備としての凝集砂濾過器は、集水装置の
上に砂利、砂、アンスラサイht積噛させ友層上から原
水に凝集剤を添刀口したものを通すことによって表層で
汚濁物貞を除去するものであり、汚濁物質が蓄積するに
従って濾過損失水頭が上昇して処理量が減少する。(1) A flocculating sand filter as a pre-treatment facility removes contaminants from the surface layer by passing gravel, sand, and anthracite over the water collecting device and passing raw water with a flocculant added over the top layer. As pollutants accumulate, the filtration head loss increases and the throughput decreases.
これを回復するためには、濾過を停止して逆洗を実施し
なければ々らず、連続操業ができなかった。In order to recover from this problem, it was necessary to stop filtration and perform backwashing, making continuous operation impossible.
(2)逆洗時の濾過器全確保するため、複数基の砂濾過
器が必要であった。(2) In order to secure all the filters for backwashing, multiple sand filters were required.
(3)また、逆洗操作では濾過流路を遮断し、逆洗流路
としなければならず、このための配管や制伺弁が多く複
雑でかつ高価な機器が必要であつ之。(3) Furthermore, in the backwash operation, the filtration flow path must be shut off to create a backwash flow path, which requires a large number of piping and control valves, and requires complicated and expensive equipment.
本発明は、以上のような従来の砂濾過器の問題点を解決
することができる濾過装置を提供しようとするものであ
る。The present invention aims to provide a filtration device that can solve the problems of conventional sand filters as described above.
本発明の濾過装置は、円筒形のア過体、一方から汚濁液
が供給され他方へ汚濁質を排出し、前記濾過体の軸心だ
設けられ九濾過体の中空回転軸、同中空回転軸を軸方向
の2部分に仕切る仕切板、同仕切板の両側において中空
回転軸全貫通して設けられた流路、及び前記濾過体内に
充填さ几た汚濁物剥離用粒子を漏えている。The filtration device of the present invention includes a cylindrical filter body, a polluted liquid is supplied from one side and pollutants are discharged to the other side, a hollow rotating shaft of the filter body is provided at the axis of the filter body, and a hollow rotating shaft of the filter body is provided with a hollow rotating shaft of the filter body. A partition plate divides the filter into two parts in the axial direction, a flow path is provided on both sides of the partition plate completely penetrating the hollow rotating shaft, and dirt-removing particles filled in the filter body are leaked.
本発明において、中空回転軸内へ一方から汚濁液が供給
され、この汚濁液は回転軸を貫通する流路から中空回転
軸によって回転する濾過体内へ入り、同濾過体によって
汚濁液の濾過が行なわれる。この際、汚濁液中の微粒子
等は濾過体の内@表面に捕捉され、濾過された准ば濾過
体を通過して排出されるっ前記PFt体の内側表面に捕
捉さf′1.た微粒子等は、濾過体の回転によって底部
に至ると、充填されている汚濁物剥離用粒子と接触しな
がら回転し、上方向へ移動する。この場合、汚濁物剥離
用粒子も濾過体と共に上方へ移動するが、摩擦力と重力
の均衡がくずれると下方へすべり落ちる。この時、その
摩擦力によって、ア過体内個表面上に捕捉さf′した微
粒子等は濾過体表面から剥離されて液中に懸濁する。こ
の懸濁液は中空回転軸内の排出側へ入って、系外て排出
される。In the present invention, the polluted liquid is supplied into the hollow rotating shaft from one side, and the polluted liquid enters the filter body rotated by the hollow rotating shaft from the flow path passing through the rotating shaft, and the polluted liquid is filtered by the filter body. It will be done. At this time, fine particles in the polluted liquid are captured on the inner surface of the filter body, and the filtered liquid passes through the filter body and is discharged.F'1. When the fine particles reach the bottom by rotation of the filter, they rotate while coming into contact with the dirt removal particles filled therein, and move upward. In this case, the dirt removal particles also move upward together with the filter, but when the balance between frictional force and gravity is lost, they slide downward. At this time, due to the frictional force, the particles f' captured on the inner surface of the filter are peeled off from the filter surface and suspended in the liquid. This suspension enters the discharge side of the hollow rotating shaft and is discharged out of the system.
以上のように、濾過体の回転に伴って、その表面は自動
的に清浄化されて目詰りを起すことがなく、濾過を継続
して行なうことが可能である。As described above, as the filter rotates, its surface is automatically cleaned and no clogging occurs, allowing continuous filtration.
本発明の一実施例を第1図によって説明する。 An embodiment of the present invention will be described with reference to FIG.
1は円筒状の濾過器外筒で上部に濾過水排出口2を儂え
、前部と後部にそれぞれ軸受シール部3a、3bが設け
られている。4けステンレス金網、ステンレスに焼結金
属製等の円筒状の濾過体で、その軸心の一端は懸濁液の
回転供給管5に、その軸心の他端は懸濁微粒子の回転排
出管6にそれぞれ連結されている。前記懸濁液の回転供
給管5及び懸濁微粒子の回転排出管6は、いずれも回転
軸の役目も兼備しており、両者は仕切板7によって管の
中空部が軸と直角に隔離されるように直線状をなして連
結されている。Reference numeral 1 denotes a cylindrical filter outer cylinder, which has a filtered water outlet 2 at its upper part, and bearing seals 3a and 3b at its front and rear parts, respectively. A cylindrical filter body made of 4-piece stainless steel wire mesh, stainless steel and sintered metal, etc. One end of its axis is connected to a rotating suspension supply pipe 5, and the other end of its axis is connected to a rotating discharge pipe for suspended particles. 6, respectively. The suspension rotating supply pipe 5 and the suspended fine particle rotating discharge pipe 6 both serve as rotating shafts, and the hollow portions of the pipes are separated by a partition plate 7 at right angles to the shafts. They are connected in a straight line.
懸濁液の回転供給管5と懸濁微粒子の回転排出管6には
濾過体4の内側の仕切板7の両側において、管を貫通す
るように開孔された供給液流路8と排出液流路9とを備
えている。また懸濁液の回転供給管5と懸濁微粒子の回
転排出管6の両端はロータリージョイン)10a、10
bを介してそれぞれ、懸濁液供給管11と懸濁微粒子排
出管12に連結されている。13Fi懸濁微粒子排出管
にがん合されたプーリーで、゛図ボしないモーターに、
ベルト等で接続される。The rotating supply pipe 5 for the suspension and the rotating discharge pipe 6 for the suspended particulates have a supply liquid flow path 8 and a discharge liquid that are opened on both sides of the partition plate 7 inside the filter body 4 so as to pass through the pipes. A flow path 9 is provided. Furthermore, both ends of the suspension rotating supply pipe 5 and the suspended fine particle rotating discharge pipe 6 are rotary joints) 10a, 10.
They are respectively connected to a suspension supply pipe 11 and a suspended particulate discharge pipe 12 via b. The pulley is tightly coupled to the 13Fi suspended particulate discharge pipe, and the motor does not move freely.
Connected with a belt, etc.
14ii濾過体4の内部に充填され几砂、好ましくd、
ステンレス製の:暁結金属粉末専の粒子である。14ii Filled inside the filter body 4 with sand, preferably d,
Made of stainless steel: Made of particles exclusively made of Akatsuki metal powder.
以上の構成をもつ本実施例では、懸濁微粒子を含む液は
懸濁液供給管11、ロータリージョイン)10a及び懸
濁液回転供給管5を経て、供給液流路8から濾過体4の
内部に導かれる。In this embodiment having the above configuration, the liquid containing suspended particles passes through the suspension supply pipe 11, the rotary joint 10a, and the suspension rotary supply pipe 5, and then enters the inside of the filter body 4 from the supply liquid flow path 8. guided by.
懸濁微粒子は濾過作用によって濾過体4の内側表面に捕
捉され、清浄となった濾過液たけが濾過水排出口2から
取り出される。一方、FiA体4の内側表面に捕捉され
た懸濁微粒子は、濾過体4が回転して底部に至ると、底
部に充填された粒子14と接触し乍ら回転し上方向へ移
動する。この場合、粒子14本濾過体4と共に上方向へ
移動するが、摩擦力と重力の均衡がくずれると下方向へ
すべり落ちることとなる。この時、その摩擦力によって
濾過体4の表面に捕捉された懸濁微粒子は剥離作用を受
け、再び液中に懸濁する。この懸濁液は排出液流路9か
ら懸濁の回転排出管6に吸引され、ロータリージヨイン
ト10b、懸濁微粒子排出管12を経て、系外に排出さ
れる。The suspended particles are captured on the inner surface of the filter body 4 by the filtration action, and the purified filtrate is taken out from the filtrate outlet 2. On the other hand, when the filter body 4 rotates and reaches the bottom, the suspended particles captured on the inner surface of the FiA body 4 rotate and move upward while coming into contact with the particles 14 filled at the bottom. In this case, the 14 particles move upward together with the filter body 4, but if the balance between frictional force and gravity is lost, they will slide downward. At this time, the suspended fine particles captured on the surface of the filter body 4 are subjected to a peeling action due to the frictional force, and are suspended in the liquid again. This suspension is sucked into the suspension rotary discharge pipe 6 from the discharge liquid channel 9, passes through the rotary joint 10b and the suspended particulate discharge pipe 12, and is discharged to the outside of the system.
以上の通り、本実施例〉Cおいては、濾過体4は、回転
しながら濾過を行なうと共に、その内側表面に捕捉し几
懸濁微粒子は自動的に濾過体の内側表面から剥離きれ、
目詰りを生ずることがない。従って、逆洗等の操作を行
なうことなく、継続して濾過を行なうことができる。As described above, in this embodiment C, the filter body 4 performs filtration while rotating, and the suspended fine particles captured and suspended on its inner surface are automatically peeled off from the inner surface of the filter body.
No clogging occurs. Therefore, filtration can be continued without performing operations such as backwashing.
本発明は次の効果を奏することができる。 The present invention can have the following effects.
(1)濾過体が回転し乍ら濾過と、剥離、洗浄を繰り返
すので目詰まりが生ずる恐れはなく、長時間尤亘り自動
かつ、連続的に操業することができる。(1) Since filtration, stripping, and washing are repeated while the filter body rotates, there is no risk of clogging, and it can be operated automatically and continuously for a long time.
(2)従って、従来のように逆洗時の戸通水を確保する
複数の濾過装置が不要となる。(2) Therefore, there is no need for multiple filtration devices to ensure water flow during backwashing as in the past.
(3)装置が簡略化さnて制御用の機器を省略すること
ができる。(3) The device can be simplified and control equipment can be omitted.
第1図は本発明の一実施例の縦断面図である。
1・・・濾過器外筒、2・・・濾過水排出口、4・・・
濾過体、5・・・回転供給管、6・・・回転排出管、7
・・・仕切板、8・・・供給液流路、9・・・排出液流
路、10 a、 10 b・−・o−タリージヨイン
ト、11・・・懸濁液供給管、12・・・懸濁粒子排出
管、14・−粒子。FIG. 1 is a longitudinal sectional view of one embodiment of the present invention. 1... Filter outer cylinder, 2... Filtered water outlet, 4...
Filter body, 5... Rotating supply pipe, 6... Rotating discharge pipe, 7
... Partition plate, 8... Supply liquid flow path, 9... Discharge liquid flow path, 10 a, 10 b...o-tally joint, 11... Suspension liquid supply pipe, 12... Suspended particle discharge tube, 14.-particles.
Claims (1)
質を排出し、前記濾過体の軸心に設けられた濾過体の中
空回転軸、同中空回転軸を軸方向の2部分に仕切る仕切
板、同仕切板の両側において中空回転軸を貫通して設け
られた流路、及び前記濾過体内に充填された汚濁物剥離
用粒子を備えたことを特徴とする濾過装置。A cylindrical filter body, a polluted liquid is supplied from one side and pollutants are discharged to the other side, a hollow rotating shaft of the filter body is provided at the axis of the filter body, and the hollow rotating shaft is partitioned into two parts in the axial direction. A filtration device comprising a partition plate, a flow path provided on both sides of the partition plate passing through a hollow rotating shaft, and particles for removing contaminants filled in the filter body.
Priority Applications (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
JP10044490A JPH044007A (en) | 1990-04-18 | 1990-04-18 | Filter |
Applications Claiming Priority (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
JP10044490A JPH044007A (en) | 1990-04-18 | 1990-04-18 | Filter |
Publications (1)
Publication Number | Publication Date |
---|---|
JPH044007A true JPH044007A (en) | 1992-01-08 |
Family
ID=14274100
Family Applications (1)
Application Number | Title | Priority Date | Filing Date |
---|---|---|---|
JP10044490A Pending JPH044007A (en) | 1990-04-18 | 1990-04-18 | Filter |
Country Status (1)
Country | Link |
---|---|
JP (1) | JPH044007A (en) |
-
1990
- 1990-04-18 JP JP10044490A patent/JPH044007A/en active Pending
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