JP2002177948A - Water cleaning plant - Google Patents
Water cleaning plantInfo
- Publication number
- JP2002177948A JP2002177948A JP2000377950A JP2000377950A JP2002177948A JP 2002177948 A JP2002177948 A JP 2002177948A JP 2000377950 A JP2000377950 A JP 2000377950A JP 2000377950 A JP2000377950 A JP 2000377950A JP 2002177948 A JP2002177948 A JP 2002177948A
- Authority
- JP
- Japan
- Prior art keywords
- water
- treated
- separated
- cylinder
- double inner
- 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 97
- 238000004140 cleaning Methods 0.000 title abstract 2
- 239000007788 liquid Substances 0.000 claims abstract description 31
- 238000000926 separation method Methods 0.000 claims abstract description 22
- 239000007787 solid Substances 0.000 claims abstract description 17
- 239000002245 particle Substances 0.000 claims abstract description 7
- 230000003068 static effect Effects 0.000 claims abstract description 6
- 239000010419 fine particle Substances 0.000 claims description 31
- 239000012141 concentrate Substances 0.000 claims description 23
- 238000001914 filtration Methods 0.000 claims description 12
- 238000000746 purification Methods 0.000 claims description 9
- 238000002156 mixing Methods 0.000 claims description 8
- 239000003795 chemical substances by application Substances 0.000 claims description 7
- 238000007599 discharging Methods 0.000 claims description 6
- 238000004042 decolorization Methods 0.000 claims description 2
- 239000000463 material Substances 0.000 claims 1
- 239000002351 wastewater Substances 0.000 abstract description 2
- 230000000694 effects Effects 0.000 abstract 2
- 230000005484 gravity Effects 0.000 description 8
- 239000000701 coagulant Substances 0.000 description 4
- 239000000084 colloidal system Substances 0.000 description 2
- 239000010842 industrial wastewater Substances 0.000 description 2
- 235000008733 Citrus aurantifolia Nutrition 0.000 description 1
- 235000011941 Tilia x europaea Nutrition 0.000 description 1
- 230000004931 aggregating effect Effects 0.000 description 1
- 238000005345 coagulation Methods 0.000 description 1
- 230000015271 coagulation Effects 0.000 description 1
- 238000009795 derivation Methods 0.000 description 1
- 238000010586 diagram Methods 0.000 description 1
- 238000009434 installation Methods 0.000 description 1
- 239000004571 lime Substances 0.000 description 1
- 238000000034 method Methods 0.000 description 1
- 239000011859 microparticle Substances 0.000 description 1
- 239000008213 purified water Substances 0.000 description 1
- 230000003134 recirculating effect Effects 0.000 description 1
- 238000010992 reflux Methods 0.000 description 1
- 238000009287 sand filtration Methods 0.000 description 1
- 239000000126 substance Substances 0.000 description 1
Landscapes
- Separation Of Suspended Particles By Flocculating Agents (AREA)
- Physical Water Treatments (AREA)
Abstract
Description
【0001】[0001]
【発明の属する技術分野】本発明は、工場排水等の被処
理水を省スペースで短時間に効率良く浄化処理する浄水
装置に関するものである。BACKGROUND OF THE INVENTION 1. Field of the Invention The present invention relates to a water purification apparatus for efficiently purifying water to be treated, such as industrial wastewater, in a short space and in a short time.
【0002】[0002]
【従来の技術】従来、工場排水等の被処理水から固形
物、有機質のコロイド状物質(例えば、粒子径20μ
m、比重1.2程度)等の微粒子を除去処理するには、
砂濾過、加圧浮上槽、凝集沈殿槽等の浄水設備が使用さ
れている。2. Description of the Related Art Conventionally, solids and organic colloidal substances (for example, having a particle
m, specific gravity of about 1.2)
Water purification equipment such as sand filtration, a pressure floatation tank, and a coagulation settling tank are used.
【0003】[0003]
【発明が解決しようとする課題】従来の上記浄水設備
は、広い設置面積を必要とし、しかも、処理に長時間を
必要としている点で問題があった。The conventional water purification equipment has a problem in that it requires a large installation area and requires a long time for the treatment.
【0004】本発明は、上記従来の問題点に鑑みて提供
されたもので、工場排水等の被処理水を省スペースで短
時間に効率良く浄化処理する浄水装置を提供することを
目的としている。The present invention has been made in view of the above-mentioned conventional problems, and has as its object to provide a water purification apparatus for efficiently purifying water to be treated, such as factory wastewater, in a space-saving manner in a short time. .
【0005】[0005]
【課題を解決するための手段】上記目的を達成するた
め、本発明は、被処理水に凝集剤を添加して被処理水中
の粗大固形物を分離する粗固液分離装置と、該粗固液分
離装置で粗大固形物を分離除去した被処理水を微粒子濃
縮物と処理水とに分離する精密固液分離装置と、該精密
固液分離装置で分離された処理水に脱色剤を添加して浄
水とする脱色装置とを具備し、前記精密固液分離装置
を、筒状体からなる外筒と、この外筒の両端開口部を閉
止する一対の蓋体と、上記外筒内に配設された二重の内
筒と、この二重の内筒内に配設された中心筒と、上記外
筒に沿って気泡を発生させつつ被処理水を旋回流動させ
るようにこの外筒内に気体を混入した被処理水を供給す
る外側渦流発生手段と、上記被処理水の旋回流動に応じ
て作用する遠心力により分離された微粒子濃縮物を外部
に排出する濃縮物排出路と、上記微粒子濃縮物が分離さ
れた分離水を上記二重の内筒内に透過させ、その際、上
記分離水中の微粒子を前記被処理水中の気泡により捕集
させて濾過分離させるために前記二重の内筒に形成した
多数の透孔からなる濾過部と、上記二重の内筒内に透過
した分離水を気泡と共に前記と逆方向に旋回流動させる
ことにより、その径方向に生じる静圧差に応じて上記気
泡を中心部側に移動させて気水混合渦流を生成し、この
気水混合渦流により微粒子を集中させて二重の内筒の上
部周囲から外側へ排出させて微粒子濃縮物として前記濃
縮物排出路から排出し、残りの分離水を二重の内筒の上
部中央から循環路を経て再び前記二重の内筒の間に下部
から接線方向に還流させる内側渦流発生手段と、前記二
重の内筒内に配設され、前記気水混合渦流中の気泡によ
り微粒子を捕集分離させた処理水を下方から外部に導出
する中心筒とで構成したものである。SUMMARY OF THE INVENTION In order to achieve the above object, the present invention relates to a crude solid-liquid separation apparatus for adding a flocculant to treated water to separate coarse solids in the treated water. A precision solid-liquid separation device that separates the water to be treated, into which fine solids have been separated and removed by a liquid separation device, into fine particle concentrates and treated water, and a decolorizing agent is added to the treated water separated by the precision solid-liquid separation device. A decolorizing device for purifying water, and disposing the precision solid-liquid separator in an outer cylinder formed of a cylindrical body, a pair of lids for closing both ends of the outer cylinder, and the inside of the outer cylinder. A double inner cylinder is provided, a center cylinder disposed in the double inner cylinder, and an inner cylinder inside the outer cylinder so as to swirl and flow the water to be treated while generating bubbles along the outer cylinder. Vortex generating means for supplying the water to be treated mixed with gas to the outside, and a centrifugal force acting according to the swirling flow of the water to be treated. A concentrate discharge passage for discharging the separated fine particle concentrate to the outside, and separated water from which the fine particle concentrate has been separated is allowed to pass through the double inner cylinder, and at this time, the fine particles in the separated water are covered with the separated water. A filtration unit comprising a large number of through holes formed in the double inner cylinder for collecting and filtering and separating by bubbles in the treated water, and separating the separated water permeated into the double inner cylinder together with the bubbles with the above. By swirling in the opposite direction, the air bubbles are moved to the center side according to the static pressure difference generated in the radial direction to generate a gas-water mixing vortex, and the fine particles are concentrated by the gas-water mixing vortex and doubled. Discharged from the upper part of the inner cylinder to the outside from the upper part of the inner cylinder and discharged as a fine particle concentrate from the concentrate discharge path, and the remaining separated water is again circulated from the upper center of the double inner cylinder via the circulation path to the double inner cylinder. Eddy current generated by tangential reflux from below in the middle And the step is disposed in the double inner tube of, in which the treated water fine particles are collected separated by bubbles of said steam-water mixing vortex flow is constituted by a central cylinder to derive from the lower to the outside.
【0006】[0006]
【発明の実施の形態】以下、本発明の実施の形態を図面
に基いて説明する。図1は本発明の浄水装置全体の概略
図、図2の(A)は精密固液分離装置の拡大説明図、
(B)は中心筒上部での微粒子捕集分離の様子を示す説
明図である。Embodiments of the present invention will be described below with reference to the drawings. FIG. 1 is a schematic view of the entire water purification apparatus of the present invention, FIG. 2A is an enlarged explanatory view of a precision solid-liquid separation apparatus,
(B) is an explanatory view showing a state of particulate collection and separation at the upper part of the center cylinder.
【0007】図1において、1は粗固液分離装置、2は
精密固液分離装置、3は脱色装置を示している。In FIG. 1, reference numeral 1 denotes a crude solid-liquid separator, 2 denotes a precision solid-liquid separator, and 3 denotes a decolorizer.
【0008】粗固液分離装置1は、被処理水に凝集剤を
添加して被処理水中の粗大固形物を凝集分離するもの
で、図1に示すように、分離槽1aと、この分離槽1a
に被処理水を導入する導入路1bと、この導入路1bの
途中に設けた凝集剤添加部1cと、分離槽1aで凝集分
離された粗大固形物を排出する排出路1dと、分離槽1
aから被処理水を導出する導出路1eとを有する。The coarse-solid-liquid separation device 1 is a device for adding a coagulant to water to be treated and aggregating and separating coarse solids in the water to be treated. As shown in FIG. 1a
, A coagulant addition section 1c provided in the middle of the introduction path 1b, a discharge path 1d for discharging coarse solids coagulated and separated in the separation tank 1a, and a separation tank 1b.
and a derivation path 1e for deriving water to be treated from a.
【0009】精密固液分離装置2は、前記粗固液分離装
置1で粗大固形物を分離除去した被処理水を微粒子濃縮
物と処理水とに分離するためのもので、図2に示すよう
に、筒状体からなる外筒2aと、この外筒2aの両端開
口部を閉止する一対の蓋体2b、2cと、上記外筒2a
内に配設された二重の内筒2d、2eと、この二重の内
筒2d、2e内に配設された中心筒2fと、上記外筒2
aに沿って気泡を発生させつつ被処理水を旋回流動させ
るようにこの外筒2a内に気体を混入した被処理水を供
給する外側渦流発生手段2gと、上記被処理水の旋回流
動に応じて作用する遠心力により分離された微粒子濃縮
物を外部に排出する濃縮物排出路2hと、上記微粒子濃
縮物が分離された分離水を上記二重の内筒2d、2e内
に透過させ、その際、上記分離水中の微粒子を前記被処
理水中の気泡により捕集させて濾過分離させるために前
記二重の内筒2d、2eに形成した多数の透孔からなる
濾過部2i、2jと、上記二重の内筒2d、2e内に透
過した分離水を気泡と共に前記と逆方向に旋回流動させ
ることにより、その径方向に生じる静圧差に応じて上記
気泡を中心部側に移動させて気水混合渦流を生成し、こ
の気水混合渦流により微粒子を集中させて二重の内筒2
d、2eの上部周囲から外側へ排出させて微粒子濃縮物
として前記濃縮物排出路2hから排出し、残りの分離水
を二重の内筒2d、2eの上部中央から循環路2kを経
て再び前記二重の内筒2d、2eの間に下部から接線方
向に還流させる内側渦流発生手段2mと、前記二重の内
筒2d、2e内に配設され、前記気水混合渦流中の気泡
により微粒子を捕集分離させた処理水を下方から外部に
導出する中心筒2fとで構成したものである。The precision solid-liquid separator 2 is for separating the water to be treated, from which coarse solids have been separated and removed by the coarse and solid-liquid separator 1, into fine particle concentrates and treated water, as shown in FIG. An outer cylinder 2a formed of a cylindrical body, a pair of lids 2b and 2c for closing both ends of the outer cylinder 2a, and the outer cylinder 2a
The inner cylinder 2d, 2e disposed in the inner cylinder, the center cylinder 2f disposed in the inner cylinder 2d, 2e, and the outer cylinder 2
a outer vortex flow generating means 2g for supplying the water to be treated mixed with gas into the outer cylinder 2a so that the water to be treated is swirled while generating air bubbles along the line a. And a concentrate discharge passage 2h for discharging the fine particle concentrate separated by centrifugal force acting outside, and the separated water from which the fine particle concentrate has been separated is passed through the double inner cylinders 2d and 2e. At this time, in order to collect the fine particles in the separated water by bubbles in the water to be treated and to separate them by filtration, the filtration units 2i, 2j formed of a large number of through holes formed in the double inner cylinders 2d, 2e; The separated water permeated into the double inner cylinders 2d and 2e is swirled in the opposite direction together with the air bubbles to move the air bubbles toward the center according to the static pressure difference generated in the radial direction. A mixed vortex is generated, and this gas-water mixed vortex Ri to concentrate the microparticles double inner cylinder 2
d and 2e are discharged to the outside from the upper periphery and discharged as fine particle concentrate from the concentrate discharge passage 2h, and the remaining separated water is again passed through the circulation passage 2k from the upper center of the double inner cylinders 2d and 2e. Inside vortex generating means 2m for tangentially recirculating from the lower portion between the double inner cylinders 2d and 2e, and fine particles formed in the double inner cylinders 2d and 2e by bubbles in the gas-water mixed vortex. And a central tube 2f that leads the treated water from which water has been collected and separated to the outside from below.
【0010】上記二重の内筒2d、2eは、外筒2a内
の上下方向全長に亘って配設されており、上部を円錐状
に縮少させて微粒子の分離効率を高めるように構成され
ている。The double inner cylinders 2d and 2e are disposed over the entire length of the outer cylinder 2a in the vertical direction, and are configured so that the upper part is reduced to a conical shape to increase the efficiency of separating fine particles. ing.
【0011】濾過部2i、2jは、二重の内筒2d、2
eの円錐状部から上部に形成されている。The filtration units 2i and 2j are composed of double inner cylinders 2d and 2d.
The upper part is formed from the conical part of e.
【0012】中心筒2fは、二重の内筒2d、2e内
で、濾過部2i、2jよりも下部に配設されている。こ
の中心筒2fの上端は、図2の(B)に示すように、円
錐状部2f'としてあり、その中心に下方へ垂下させた
垂下筒2f"を有する。そして、この中心筒2fの下部
には処理水の導出路2nが接続されている。The center tube 2f is disposed below the filtration units 2i and 2j in the double inner tubes 2d and 2e. As shown in FIG. 2B, the upper end of the center tube 2f is formed as a conical portion 2f ', and has a drooping tube 2f "which is drooped downward at the center thereof, and a lower portion of the center tube 2f. Is connected to an outlet 2n for treated water.
【0013】外側渦流発生手段2gは、粗固液分離装置
1で粗大固形物が分離除去された被処理水を導出路1e
に接続された導入路2oから外筒2a内にその下部から
接線方向に導入して外筒2a内に旋回流を発生させるも
ので、その導入路2oの途中にはエア等の気体混入部2
pを設けている。The outer vortex flow generating means 2g supplies the treated water from which coarse solids have been separated and removed by the coarse / solid liquid separating apparatus 1 to an outlet path 1e.
A tangential flow is introduced into the outer cylinder 2a from the lower part thereof through the introduction path 2o connected to the outer cylinder 2a to generate a swirling flow in the outer cylinder 2a.
p is provided.
【0014】脱色装置3は、精密固液分離装置2で分離
された処理水に適宜の脱色剤(例えば、石灰等)を添加
して脱色処理するもので、図1に示すように、脱色処理
槽3aと、この脱色処理槽3aに精密固液分離装置2の
導出路2nから導出された処理水を導入する導入路3b
と、この導入路3bの途中に設けた脱色剤添加部3c
と、脱色処理槽3aから浄水を導出する導出路3dとを
有する。The decolorizing device 3 performs a decoloring process by adding an appropriate decolorizing agent (eg, lime) to the treated water separated by the precision solid-liquid separating device 2. As shown in FIG. A tank 3a and an introduction path 3b for introducing the treated water derived from the discharge path 2n of the precision solid-liquid separation device 2 into the decolorization treatment tank 3a.
And a decolorizing agent adding section 3c provided in the middle of the introduction path 3b.
And an outlet 3d for extracting purified water from the decolorizing tank 3a.
【0015】本発明の浄水装置の実施形態は、以上の構
成からなり、次に動作を説明する。The embodiment of the water purification apparatus of the present invention has the above-described configuration, and the operation will be described next.
【0016】先ず、粗固液分離装置1では、被処理水中
に含まれている粗大固形物を分離除去することが行われ
る。この分離除去を促進するために、凝集剤が添加され
る。次に、粗固液分離装置1で粗大固形物を分離除去し
た被処理水を精密固液分離装置2に導入する。ここで
は、先ず、外側渦流発生手段2gにより外筒2a内で被
処理水を旋回させることによって生じる遠心力および静
圧差に応じて、被処理水中に含まれた比重の大きな微粒
子を渦流の外方側に移動させて上部の濃縮物排出路2か
ら外部に排出するとともに、被処理水中に含まれた比重
の小さな微粒子を渦流の中心部側に移動させ、この中心
部に生成された気泡とともに上記比重の小さな微粒子を
上昇させて上方の濃縮物排出路2から外部に排出する。
そして、外側渦流発生手段2gにより比重の大きい微粒
子が分離されることによって生成された分離水が、二重
の内筒2d、2eの濾過部2i、2jを透過する際に、
分離水中の微粒子が気泡に捕集されることにより、この
透過水中に比重の小さい微粒子が帯同されることが防止
される。即ち、二重の内筒2d、2eの濾過部2i、2
jでは、多数の透孔を覆うように付着した気泡に上記微
粒子が捕集されることにより、濾過が良好に行われる。First, in the crude solid-liquid separation device 1, coarse solids contained in the water to be treated are separated and removed. A coagulant is added to facilitate this separation and removal. Next, the water to be treated, from which coarse solids have been separated and removed by the crude solid-liquid separator 1, is introduced into the precision solid-liquid separator 2. Here, first, fine particles having a large specific gravity contained in the water to be treated are discharged outward from the vortex in accordance with the centrifugal force and the static pressure difference generated by swirling the water to be treated in the outer cylinder 2a by the outer vortex generating means 2g. And discharged to the outside from the concentrate discharge path 2 at the upper side, and the fine particles having a low specific gravity contained in the water to be treated are moved to the center of the vortex, and the air bubbles generated in the center together with the air bubbles generated at the center Fine particles having a small specific gravity are lifted and discharged to the outside from the concentrate discharge passage 2 above.
Then, when the separated water generated by the separation of the fine particles having a large specific gravity by the outer vortex flow generating means 2g passes through the filtration units 2i and 2j of the double inner cylinders 2d and 2e,
Since the fine particles in the separated water are collected by the bubbles, the fine particles having a small specific gravity are prevented from being entrained in the permeated water. That is, the filtration units 2i, 2 of the double inner cylinders 2d, 2e
In j, the fine particles are collected by bubbles attached so as to cover a large number of through-holes, so that the filtration is performed well.
【0017】また、内側渦流発生手段2mは、二重の内
筒2d、2eの内側に外側とは逆方向の渦流を発生する
ように構成しているため、濾過部2i、2jを透過した
分離水が旋回流動することにより生じる遠心力に応じて
比重の大きい微粒子が外側へ順次分離され、上部から順
次濃縮物排出路2hを経て排出される。二重の内筒2
d、2eの間及び内側に透過した水は、透過水中に含ま
れた気泡により微粒子を捕集しつつ気水混合渦流を形成
して上昇し、循環路2kから再び二重の内筒2d、2e
の間に還流され、濾過が行われる。中心筒2fの上部で
は、図2の(B)に示すように、円錐状部2f'の上面
に気泡が付着して、その気泡が中心の垂下筒2f"から
下方へ流下する水に含まれている微粒子を捕捉し、中心
部に形成されている気水混合渦流に合体して上昇し、前
記循環路2kに至る。一方、垂下筒2f"内を経た水
は、残存する気泡を中心部の気水混合渦流に放出しなが
ら中心筒2fを流下して下部の導出路2nから導出され
る。The inner vortex generating means 2m is configured to generate a vortex in the opposite direction to the outer side inside the double inner cylinders 2d and 2e. Fine particles having a large specific gravity are sequentially separated to the outside in accordance with the centrifugal force generated by the swirling flow of water, and are sequentially discharged from the top through the concentrate discharge path 2h. Double inner cylinder 2
The water permeated between and inside d and 2e rises by forming a gas-water mixed vortex while collecting fine particles by bubbles contained in the permeated water, and again from the circulation path 2k, the double inner cylinder 2d, 2e
During which time filtration is performed. In the upper part of the central cylinder 2f, as shown in FIG. 2B, air bubbles adhere to the upper surface of the conical portion 2f ', and the air bubbles are contained in water flowing down from the central hanging cylinder 2f ". The water traps the trapped fine particles and rises together with the air-water mixing vortex formed in the center to reach the circulation path 2k. On the other hand, the water passing through the hanging cylinder 2f " And flows down the central cylinder 2f while being discharged into the air-water mixed vortex, and is drawn out from the lower outlet path 2n.
【0018】上記導出路2nから導出された処理水は、
導入路3bから脱色処理槽3aに導入され、途中の脱色
剤添加部3cから脱色剤が添加され、脱色処理槽3a内
で脱色処理された後、導出路3dから導出される。The treated water led out from the outlet 2n is:
After being introduced into the decolorizing treatment tank 3a from the introduction path 3b, the decolorizing agent is added from the decolorizing agent adding section 3c on the way, and subjected to the decolorizing treatment in the decolorizing processing tank 3a, it is led out from the lead-out path 3d.
【0019】[0019]
【発明の効果】以上説明したように、本発明によれば、
粗固液分離装置で被処理水中の粗大固形物を分離除去し
た後、精密固液分離装置で微粒子やコロイド粒子を精密
に分離除去しているため、精密固液分離装置の過負荷を
防止して長時間の連続運転を可能とすることができ、最
後に脱色装置で脱色処理して浄水化することができる。
また、精密固液分離装置においては、旋回流動による遠
心力分離作用と、旋回方向が逆の内外二重の渦流発生手
段による静圧落差及び気泡混入による微粒子捕集作用と
により、構造が簡単で比重の小さい微粒子やコロイド粒
子の分離除去に好適な装置を得ることができ、工場排水
等の被処理水を省スペースで短時間に効率良く浄化処理
する浄水装置を提供することができる。As described above, according to the present invention,
After the coarse solids in the water to be treated are separated and removed by the coarse and solid-liquid separator, the fine solids and colloid particles are precisely separated and removed by the precision solid-liquid separator to prevent overload of the precision solid-liquid separator. For a long period of time, continuous operation is possible, and finally, the water can be purified by decolorizing treatment with a decoloring device.
In the precision solid-liquid separation device, the structure is simple due to the centrifugal force separating action by the swirling flow and the static pressure drop by the inner and outer double vortex generating means in the opposite swirling direction and the fine particle collecting action by the inclusion of bubbles. An apparatus suitable for separating and removing fine particles and colloid particles having a small specific gravity can be obtained, and a water purification apparatus for efficiently purifying water to be treated such as industrial wastewater in a short time in a small space can be provided.
【図1】本発明の浄水装置全体の概略図。FIG. 1 is a schematic diagram of the entire water purification apparatus of the present invention.
【図2】(A)は精密固液分離装置の拡大説明図、
(B)は中心筒上部での微粒子捕集分離の様子を示す説
明図。FIG. 2A is an enlarged explanatory view of a precision solid-liquid separation device,
(B) is an explanatory view showing the state of particulate collection and separation at the upper part of the center cylinder.
1 粗固液分離装置 1a 分離槽 1b 導入路 1c 凝集剤添加部 1d 固形物排出路 1e 導出路 2 精密固液分離装置 2a 外筒 2b、2c 蓋体 2d、2e 二重の内筒 2f 中心筒 2f' 円錐状部 2f" 垂下筒 2g 外側渦流発生手段 2h 濃縮物排出路 2i、2j 濾過部 2k 循環路 2m 内側渦流発生手段 2n 導出路 2o 導入路 2p 気体混入部 3 脱色装置 3a 脱色処理槽 3b 導入路 3c 脱色剤添加部 3d 導出路 DESCRIPTION OF SYMBOLS 1 Coarse solid-liquid separation apparatus 1a Separation tank 1b Introduction path 1c Coagulant addition part 1d Solid discharge path 1e Outlet path 2 Precision solid-liquid separation apparatus 2a Outer cylinder 2b, 2c Lid 2d, 2e Double inner cylinder 2f Center cylinder 2f 'conical portion 2f "hanging tube 2g outer vortex generating means 2h concentrate discharge path 2i, 2j filtering section 2k circulating path 2m inner vortex generating means 2n outlet path 2o introduction path 2p gas mixing section 3 decolorizing device 3a decolorizing treatment tank 3b Introductory path 3c Decolorizing agent addition section 3d Outgoing path
───────────────────────────────────────────────────── フロントページの続き Fターム(参考) 4D015 BA19 BA23 CA20 EA02 FA13 4D037 AA11 AB02 BA03 CA08 4D062 BA19 BA23 CA20 EA02 FA13 ──────────────────────────────────────────────────続 き Continued on the front page F term (reference) 4D015 BA19 BA23 CA20 EA02 FA13 4D037 AA11 AB02 BA03 CA08 4D062 BA19 BA23 CA20 EA02 FA13
Claims (1)
の粗大固形物を分離する粗固液分離装置と、該粗固液分
離装置で粗大固形物を分離除去した被処理水を微粒子濃
縮物と処理水とに分離する精密固液分離装置と、該精密
固液分離装置で分離された処理水に脱色剤を添加して浄
水とする脱色装置とを具備し、 前記精密固液分離装置を、筒状体からなる外筒と、この
外筒の両端開口部を閉止する一対の蓋体と、上記外筒内
に配設された二重の内筒と、この二重の内筒内に配設さ
れた中心筒と、上記外筒に沿って気泡を発生させつつ被
処理水を旋回流動させるようにこの外筒内に気体を混入
した被処理水を供給する外側渦流発生手段と、上記被処
理水の旋回流動に応じて作用する遠心力により分離され
た微粒子濃縮物を外部に排出する濃縮物排出路と、上記
微粒子濃縮物が分離された分離水を上記二重の内筒内に
透過させ、その際、上記分離水中の微粒子を前記被処理
水中の気泡により捕集させて濾過分離させるために前記
二重の内筒に形成した多数の透孔からなる濾過部と、上
記二重の内筒内に透過した分離水を気泡と共に前記と逆
方向に旋回流動させることにより、その径方向に生じる
静圧差に応じて上記気泡を中心部側に移動させて気水混
合渦流を生成し、この気水混合渦流により微粒子を集中
させて二重の内筒の上部周囲から外側へ排出させて微粒
子濃縮物として前記濃縮物排出路から排出し、残りの分
離水を二重の内筒の上部中央から循環路を経て再び前記
二重の内筒の間に下部から接線方向に還流させる内側渦
流発生手段と、前記二重の内筒内に配設され、前記気水
混合渦流中の気泡により微粒子を捕集分離させた処理水
を下方から外部に導出する中心筒とで構成したことを特
徴とする浄水装置。1. A crude solid-liquid separator for adding a flocculant to treated water to separate coarse solids in the treated water, and a treated solid water separated from the treated solids by the coarse solid-liquid separator. A precision solid-liquid separation device for separating into fine particle concentrate and treated water, and a decolorization device for adding a decolorizing agent to the treated water separated by the precision solid-liquid separation device to purify the water; The separating device comprises an outer cylinder formed of a cylindrical body, a pair of lids for closing both ends of the outer cylinder, a double inner cylinder disposed in the outer cylinder, and a double inner cylinder. A central cylinder disposed in the cylinder, and an outer vortex flow generating means for supplying the water to be treated mixed with gas into the outer cylinder so as to swirl and flow the water to be treated while generating bubbles along the outer cylinder. And a concentrate discharging device for discharging the fine particle concentrate separated by centrifugal force acting according to the swirling flow of the water to be treated to the outside. Channel, the separated water from which the fine particle concentrate is separated is allowed to pass through the double inner cylinder, and at this time, the fine particles in the separated water are collected by bubbles in the water to be treated and filtered and separated. A filtration section consisting of a large number of through holes formed in the double inner cylinder, and the separated water permeated into the double inner cylinder is swirled in the opposite direction to the above together with the bubbles, thereby being generated in the radial direction. The air bubbles are moved toward the center according to the static pressure difference to generate a gas-water mixing vortex, and the particles are concentrated by the gas-water mixing vortex and discharged from the upper periphery of the double inner cylinder to the outside to concentrate the particles. Inner vortex flow generating means for discharging the remaining separated water from the concentrate discharge passage as a material and returning the remaining separated water from the upper center of the double inner cylinder via the circulation path and again tangentially from the lower portion between the double inner cylinders And the air-water mixing vortex disposed in the double inner cylinder and A water purification device, comprising: a central cylinder that guides treated water, in which fine particles are collected and separated by air bubbles in a flow, to the outside from below.
Priority Applications (1)
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JP2000377950A JP2002177948A (en) | 2000-12-12 | 2000-12-12 | Water cleaning plant |
Applications Claiming Priority (1)
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JP2000377950A JP2002177948A (en) | 2000-12-12 | 2000-12-12 | Water cleaning plant |
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JP2002177948A true JP2002177948A (en) | 2002-06-25 |
Family
ID=18846602
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Cited By (3)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
KR100801981B1 (en) * | 2007-11-19 | 2008-02-12 | (주)경북환경개발 | Vortex type high efficiency pressurized solid-liquid separator |
KR101433820B1 (en) | 2012-06-04 | 2014-08-26 | 조성현 | Pressure floating device with micro bubble |
CN105330062A (en) * | 2015-11-11 | 2016-02-17 | 江苏华达环境工程有限公司 | Modular internal circulation floatation-filtration device |
-
2000
- 2000-12-12 JP JP2000377950A patent/JP2002177948A/en active Pending
Cited By (3)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
KR100801981B1 (en) * | 2007-11-19 | 2008-02-12 | (주)경북환경개발 | Vortex type high efficiency pressurized solid-liquid separator |
KR101433820B1 (en) | 2012-06-04 | 2014-08-26 | 조성현 | Pressure floating device with micro bubble |
CN105330062A (en) * | 2015-11-11 | 2016-02-17 | 江苏华达环境工程有限公司 | Modular internal circulation floatation-filtration device |
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