JPS58143860A - Floating separation apparatus - Google Patents
Floating separation apparatusInfo
- Publication number
- JPS58143860A JPS58143860A JP57025636A JP2563682A JPS58143860A JP S58143860 A JPS58143860 A JP S58143860A JP 57025636 A JP57025636 A JP 57025636A JP 2563682 A JP2563682 A JP 2563682A JP S58143860 A JPS58143860 A JP S58143860A
- Authority
- JP
- Japan
- Prior art keywords
- flotation
- tank
- floating
- inclined plate
- sediment
- 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.)
- Granted
Links
Landscapes
- Physical Water Treatments (AREA)
Abstract
Description
【発明の詳細な説明】
この発明は、固液分離と行なう浮上分離装置に関し、浮
上分離槽内の浮上筒の外周に螺旋形傾斜板を設け、沈降
物の沈降距離を短かくして沈降時(8)を短縮するよう
にし、沈降物さ浮上物との混合全防止するとともに、沈
4物の完全分離ケ図り。DETAILED DESCRIPTION OF THE INVENTION The present invention relates to a flotation device for solid-liquid separation, in which a spiral inclined plate is provided around the outer periphery of a flotation cylinder in a flotation tank to shorten the settling distance of sediment and to ), to completely prevent the mixing of sediment and floating materials, and to completely separate the sediment.
固液分離が効率的に行なえるようにしたものである。This allows efficient solid-liquid separation.
一般に、尚液分離を行なう浮上分離法は、水中に懸濁し
た微細な固体や液体粒子をそのままあるいは気泡に付着
させて浮上させ、浮上物を濃縮分離するとともに、その
下部に清澄水を得る一種の工学的操作であり、含油廃水
処理、下水処理、下水汚泥の濃縮などの水処理分野のほ
か1石炭工業や繊維工業などにおいて広く応用されてい
る技術である。In general, the flotation separation method that separates liquid is a type of method in which fine solids and liquid particles suspended in water are floated as they are or attached to air bubbles, and the floating substances are concentrated and separated, and clear water is obtained at the bottom. It is an engineering operation that is widely applied in water treatment fields such as oil-containing wastewater treatment, sewage treatment, and sewage sludge thickening, as well as in the coal industry and textile industry.
そして、この棟浮十分離法による浮子分離装置rイでは
、一般に、浮止分離槽、浮土物掻石機、浮土物欣田口、
原水流入口、空気吹込機などを備え、処理すべき原水を
そのままあるいは空気、加圧水等を混合して浮上分離槽
の槽底より送入し、懸濁物に微細な気泡を付着させるな
どして漸次水面土に浮上させたのち、これを掻117!
機により掻き集める古ともに、清澄水は別途配管により
収集するようにしている。The float separation device using this ridge-floating method generally includes a floating separation tank, a floating earth scraper, a floating earth excavator,
Equipped with a raw water inlet, an air blower, etc., the raw water to be treated is fed through the bottom of the flotation tank either as is or mixed with air, pressurized water, etc., and fine air bubbles are attached to the suspended matter. After gradually raising it to the surface of the water, I scratched it 117 times!
Both old and clear water is collected using a machine, and clear water is collected through a separate pipe.
ここで、前述の浮上分離操作においては、浮遊物をすべ
て浮上させて完全な清澄水を得ることが理想であるが、
−1″i1(浮上せrに沈降するものかあリ、その結果
、十分々清澄水を得ることが困難と々す、浮上物の回r
1y率を低下させる結果となっている。こn、ば、浮子
分離・醜内において、浮上しつつある粒子と沈降しつつ
ある粒子上が、その比重差や気泡の付着の有無などによ
って同時に生成し、しかも、この両者が混在して71流
を起こすためであり、さらVこ、沈降する粒子の沈降速
度が比較的小さいため、粒子の沈降と浮上とが同一場所
で同時に起こるためである。In the above-mentioned flotation separation operation, it is ideal to float all floating objects and obtain completely clear water.
-1"i1 (floating objects may settle on the surface of the surface, and as a result, it is difficult to obtain sufficient clear water.
This results in a decrease in the 1y rate. In this case, in the float separation/ugly, particles that are floating and particles that are settling are generated at the same time due to the difference in specific gravity and the presence or absence of air bubbles attached, and moreover, when these two are mixed, 71 This is to create a flow, and because the settling velocity of the settling particles is relatively low, the settling and floating of the particles occur simultaneously at the same location.
そこで、従来より、沈降物を除去するために、浮上分離
槽の槽底に沈降物損117機を設け、これを回転駆動し
、沈降物を掻き染めて槽底より取り出す力演が採られて
いる。しかし、この場合、動力を要するのみならず5構
造が複雑さなり、必らずしも満足すべきものではない。Therefore, in order to remove the sediment, a conventional method has been to install a sediment removal machine at the bottom of the flotation tank and drive it to rotate to dye the sediment and take it out from the tank bottom. There is. However, in this case, not only is power required, but the structure is also complicated, which is not necessarily satisfactory.
この発明は、前記の点に留意し、浮上分離槽内の浮上面
の外周に螺旋形傾斜(升を設け、効率的な同液分離が行
なえるようVこしたものであり、つきにこの発明を、そ
の1実施例全丁した図面とともVC詳卸1に説明する。This invention takes the above points into consideration, and provides a spiral slope (square) on the outer periphery of the floating surface in a flotation separation tank, and forms a V-shape for efficient separation of the same liquid. will be explained in VC Detail 1 along with the complete drawings of one embodiment.
図面において、(1)は土面が開口され、た土工方向の
円筒状の浮上分離槽、(2)は浮上分離槽(1)の底部
勿構成する漏斗状の槽底部であり、底栓(,3)2介し
て沈解物収用口(りに連)角び九でいる。(5)は浮−
に分離槽(υ内に同軸的に設けられ内部に浮十室を構成
する土工方向の浮上筒であり、その上端の浮上口(0)
が浮上分離槽(1)内の上部に開口されるとともに、下
端部が浮上分離槽(])の槽壁を負通した流入管(7)
ンこ連通され、懸濁水、加圧水、空気などが流入管(7
)より浮上面(5)内に流入される。(8)は浮上筒(
5)の外周に一体にかつ等I11]隔に設けられ浮上分
離槽(1)内と土工方向に5段に分割する4枚の螺旋形
傾斜板であり、各傾斜級(8)はそれぞれ60’以上の
傾斜角を有し、浮上分離槽(1)の槽底に向かって形成
されており、各傾斜板(8)間にはそj7ぞれ槽底に向
かう螺旋状の沈降室が構FM、さ力、前記浮土室さ分m
されるものである。(9N’;を浮」−分離槽(1)の
上端(lこ設けられ下面に複数枚のコム製のへら状掻胞
イゑ(IQが放射状に設けらf″した浮土物掻l伐機で
あり、電動機(11)の駆動により掻胞機(9)が回転
されると、浮上分#槽〜υの止面の浮上物が掻き収られ
る。(12)は浮上分離槽jlJの上部に形成され掻欣
機(9)で掻き収られた浮上物ヲ収り出す浮上物排出口
、(j3)は先端の敢出口(j’l)’が各傾斜1fi
(8)の下面の近傍にそれぞれ開口された5木の清澄
水賎出管であり、Gllヌ出管(13Iはそnぞれ集合
管(14Jに煮続され、さらに排水管1」5)に連結さ
れている。In the drawing, (1) is a cylindrical flotation tank with an open soil surface facing the earthwork direction, and (2) is a funnel-shaped tank bottom that forms the bottom of the flotation tank (1), with a bottom plug ( , 3) The sediment collection port is located at the angle of 9 through 2. (5) is float-
Separation tank (This is a flotation tube in the earthwork direction that is installed coaxially within υ and constitutes a floating chamber inside, and the flotation port (0) at the upper end
is opened at the upper part of the flotation tank (1), and the lower end passes through the tank wall of the flotation tank (]).
Suspended water, pressurized water, air, etc. are connected to the inflow pipe (7).
) into the air bearing surface (5). (8) is the levitation tube (
5) are installed on the outer periphery of the flotation tank (1) at equal intervals and are divided into 5 stages in the flotation separation tank (1) and in the earthwork direction, and each slope class (8) is 60 The flotation tank (1) has an inclination angle of more than FM, force, the floating earth chamber size m
It is something that will be done. (9N') - A floating debris scraping machine with multiple spatula-shaped combs (IQ installed radially) on the upper end of the separation tank (1) and the lower surface. When the scraper (9) is rotated by the drive of the electric motor (11), the floating matter on the stop surface of the floating fraction tank #~υ is scraped off. The floating object discharge port which collects the formed floating objects and scraped by the scraping machine (9), (j3) is a floating object outlet (j'l)' at the tip of each slope 1fi.
(8) There are 5 clear water drain pipes each opened near the bottom surface, and each Gll drain pipe (13I is connected to a collecting pipe (14J, and a drain pipe 1"5). is connected to.
つぎに、前記実施例の動作について説明する。Next, the operation of the embodiment will be explained.
捷ず、流入管(7)より懸濁水、加圧水、空気などが送
り込′まれでくる々、これが、浮上筒(5)内を上昇す
る間に微細気泡を付着した粒子間々清澄水との混合物と
なり、浮上口(6)より浮上分離槽(1)内に流出され
る。そして、浮上口(6)より流出された混合液のうち
、浮上物は、浮」二分離僧(υの上面に達すると、電動
機111により回転する掻帽引9)Kより掻き取られて
排出口(121より排出される。一方2浮上口(6)よ
り流出された混合液のうち、その比重が比較的太なるも
の、気泡の付Nが不十分なもの等の沈降物d6)は、液
中を沈降し、各傾斜g!<8)上に沈降して傾斜板(8
)上rすべって下降し、順次槽底に案内さn、槽底部(
2)に堆積される。この槽底部(2)の槽底部11物・
、]6)は5底栓(:3)を開くことにより沈降物■出
口(4)より回収される。Suspended water, pressurized water, air, etc. are sent through the inflow pipe (7) without being separated, and as they rise in the flotation tube (5), particles with fine air bubbles attached thereto are mixed with clear water. and flows out into the flotation separation tank (1) from the flotation port (6). Of the mixed liquid flowing out from the flotation port (6), the floating objects are scraped off by the float (on reaching the upper surface of υ, the scraper 9 rotated by the electric motor 111) and disposed of. It is discharged from the outlet (121). On the other hand, among the mixed liquids discharged from the 2 flotation ports (6), sediments d6), such as those whose specific gravity is relatively thick and those whose air bubbles are insufficiently attached, are Sediment in the liquid, each slope g! <8) Sink onto the inclined plate (8)
) slides down and is guided to the bottom of the tank one by one.
2). This tank bottom (2) has 11 objects.
, ]6) is recovered from the sediment ■ outlet (4) by opening the five-bottom stopper (:3).
さらに、各傾斜板(8)の下面i;4(分には、その近
傍の沈降物t161がその下方の他の11:il斜伏(
8)土に沈降するため、清澄水が分離果合しており、こ
の清澄水が各麻出口(+i)’よりlヌ出管(13)お
よび集合管(14Iを介して排水管(15)より血り出
される。Furthermore, when the lower surface of each inclined plate (8) i;
8) Clear water is separated because it settles in the soil, and this clear water flows from each hemp outlet (+i)' to the drain pipe (15) through the outlet pipe (13) and the collecting pipe (14I). It bleeds more.
したがって、前記実施例によると、浮上分離槽(υ内の
浮上筒(5)の外周に4枚の螺旋形傾斜板(8)を等間
隔に設けるこさにより、浮上分離槽(υのほぼ全長に等
しい沈降物(16)の沈降距離を各傾斜板(8)により
5段に分割することができるため、各傾斜板(8)間に
前記の115 の沈降距離を形成することができ、沈
降物(]6)の沈降時間も115 に短縮でき、沈降
物tillを各傾斜法(8)上に速かに沈降させること
ができ、しかも、1頃斜板(8)土に沈降された沈1坤
物(18)は、傾斜板(8)が沈降* tuli+のす
べり落ちる安息角60°以上の1頃斜角を有するため、
傾斜板(8)土をすべり落ち、順次槽底部(2)に堆積
され、動力を用いること;’z <、捷だ、構造を複雑
にすることなく、沈1洋物([6)を容易に1伐り出す
ことかでさるものである。Therefore, according to the embodiment, by providing four spiral inclined plates (8) at equal intervals on the outer periphery of the flotation tube (5) in the flotation tank (υ), almost the entire length of the flotation tank (υ) is covered. Since the settling distance of equal sediment (16) can be divided into five stages by each inclined plate (8), the above-mentioned 115 settling distance can be formed between each inclined plate (8), and the settling distance The settling time of (]6) can also be shortened to 115 cm, and the sediment till can be quickly settled on each slope plate (8). Since the object (18) has an angle of repose of 60° or more at which the inclined plate (8) sinks and slides down,
The inclined plate (8) slides down the soil, is deposited in sequence at the bottom of the tank (2), and uses power; It is worth cutting down one tree per day.
また、浮」二面に))内の浮上室と各イ…斜伏(8)間
における沈降室さが浮子分離槽\1)内で分離して構成
される7tめ、浮上物と沈降物・J61 &の混合を防
止し、両者を効果的VC分離することかでさ、さらに、
谷1:@斜イfy(8)間に11ぞ成さ冶グこ沈降室は
浮子水流の影響を受けることが々いlでめ、極めて静的
VCC清澄水沈沈降9勿16jとの分離が行な乏−るも
のであり、しかも、この清澄水を、その(WB度のもつ
とも高いf頃斜法(8ンの下面近傍で駆り出すむ吉がで
きるため、完全な清澄水として得るこ吉がでさるもので
あり、浮土物、沈降物(16jおよび清澄水を効率的に
分離できるものである。In addition, the flotation chamber on the two sides of the float) and the settling chamber between each slope (8) are separated in the float separation tank\1), and the 7th ton consists of floating matter and sediment.・To prevent the mixing of J61 & and to effectively separate the two, furthermore,
Valley 1: @ Diagonal I fy (8) between 11 and 11 holes The sedimentation chamber is often affected by the float water flow, and is extremely static VCC Clear water sedimentation Separation from the sedimentation 9 course 16j Moreover, this clear water cannot be obtained as perfectly clear water because it can be pumped out near the bottom of the 8th slope method (which has the highest WB degree). It is highly effective and can efficiently separate floating debris, sediment (16j) and clear water.
さらVこ、前記実施例では5円筒状の浮子分離槽(υを
使用し、その水平断面を小さくすることができるため、
傾斜4fj (8)のすべり角、すなわち1頭斜角全必
然的に犬きぐとることができ、かつ、そのピンチも大き
くでさ、したがって、沈降物t161を速かに槽底部(
2)に移動させ得るものである。Furthermore, in the above embodiment, a 5-cylindrical float separation tank (υ) is used, and its horizontal cross section can be made small.
The slip angle of slope 4fj (8), that is, the slope angle can be completely swept by a dog, and the pinch is also large. Therefore, the sediment t161 can be quickly moved to the tank bottom (
2).
なお、浮上筒(5)の夕1周に設けられたイ頃斜私(8
ンは、沈l洋物(16)の量に応じて任意に増減すれば
よい。In addition, the levitation tube (5) was set up on the first lap in the evening.
The amount may be increased or decreased as desired depending on the amount of sediment (16).
以上のように、この発明の浮上分離装置によると、上下
刃向の日商状浮上分離e+ +yq vc浮十肖を配設
するとともに、浮上的の外周に沈1祥物がすべり洛ちる
程度の1頃斜角を有する螺旋形1頭斜鈑を設けることに
より、沈11’71物の沈l洋距離を短かくして沈降時
間を短縮し、全体としての沈降速度を増大させることが
でき、沈降物と浮上物との混合を確実に防止し、効率的
な分離が実現できるとともに、構造を複雑にすることな
く、捷だ動力勿要すること々く沈1坤物の完全分離を可
能にでき、さらに、傾斜板の下面の近傍に清澄水賎出管
の昨出口を開口することにより、清澄度の高い清澄水を
取り出すことかでさるものである。As described above, according to the flotation separation device of the present invention, the Japanese commercial flotation separator e+ +yq vc floats are arranged on the upper and lower blades, and at the same time, the flotation separator is arranged such that the sediments slide around the outer periphery of the flotation surface. By providing a spiral one-head slope plate with a bevel around 1, it is possible to shorten the settling distance of sediments, shorten the settling time, and increase the overall sedimentation speed. It is possible to reliably prevent the mixing of floating materials with floating materials, and achieve efficient separation, and it is possible to completely separate sedimented materials without complicating the structure and requiring no shredding power. By opening the outlet of the clear water extraction pipe near the lower surface of the inclined plate, clear water with a high degree of clarity can be taken out.
【図面の簡単な説明】
図面はこの発明の浮上分離装置の1実施例の一部切欠断
面図である。
(1)・・浮止分離槽、(5)・・・浮」−商、(8片
・・1頭斜私、(13);・・清澄水欣出肯、(1や′
・・・収出D 、 t161・・・沈1祥物。
代理人 弁理士 藤田龍太部BRIEF DESCRIPTION OF THE DRAWINGS The drawing is a partially cutaway sectional view of one embodiment of the flotation separation device of the present invention. (1)...floating separation tank, (5)...float''-commercial, (8 pieces...1 head tilted, (13);...Kiyosumizushinzuken, (1ya'
...Procurement D, t161... Shen 1 gift. Agent: Patent Attorney Ryutabe Fujita
Claims (1)
る上下刃向の浮上筒を配設し、前記浮上筒の外周に沈降
物がすべり落ちる程度の傾斜角を有し、@記浮上分離槽
の槽底に向かう螺旋形傾斜鈑を設げたことを特徴とする
浮上分離装置。 ■ 頌斜板の下面の近傍に清澄水収出管の収出口を開口
したことを特徴とする特許請求の範囲第1項に記載の浮
上分離装置。[Claims] ■ Cylindrical flotation component with vertical blades oriented = A flotation cylinder with vertical blades oriented in the tank that constitutes a flotation chamber is provided, and the levitation cylinder has an inclination that is such that sediment can slide down on the outer periphery of the flotation cylinder. 1. A flotation separation device characterized by having a spiral sloped plate having a corner and facing toward the bottom of a flotation separation tank. (2) The flotation separation device according to claim 1, wherein an outlet of the clear water outlet pipe is opened near the lower surface of the swash plate.
Priority Applications (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
JP57025636A JPS58143860A (en) | 1982-02-18 | 1982-02-18 | Floating separation apparatus |
Applications Claiming Priority (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
JP57025636A JPS58143860A (en) | 1982-02-18 | 1982-02-18 | Floating separation apparatus |
Publications (2)
Publication Number | Publication Date |
---|---|
JPS58143860A true JPS58143860A (en) | 1983-08-26 |
JPS6161866B2 JPS6161866B2 (en) | 1986-12-27 |
Family
ID=12171335
Family Applications (1)
Application Number | Title | Priority Date | Filing Date |
---|---|---|---|
JP57025636A Granted JPS58143860A (en) | 1982-02-18 | 1982-02-18 | Floating separation apparatus |
Country Status (1)
Country | Link |
---|---|
JP (1) | JPS58143860A (en) |
Cited By (2)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
US6056125A (en) * | 1997-07-08 | 2000-05-02 | U. S. Department Of Energy | Cross flow cyclonic flotation column for coal and minerals beneficiation |
CN112208959A (en) * | 2020-09-16 | 2021-01-12 | 衢州英特高分子材料有限公司 | Solid-liquid different-opening discharge type storage tank |
-
1982
- 1982-02-18 JP JP57025636A patent/JPS58143860A/en active Granted
Cited By (2)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
US6056125A (en) * | 1997-07-08 | 2000-05-02 | U. S. Department Of Energy | Cross flow cyclonic flotation column for coal and minerals beneficiation |
CN112208959A (en) * | 2020-09-16 | 2021-01-12 | 衢州英特高分子材料有限公司 | Solid-liquid different-opening discharge type storage tank |
Also Published As
Publication number | Publication date |
---|---|
JPS6161866B2 (en) | 1986-12-27 |
Similar Documents
Publication | Publication Date | Title |
---|---|---|
US7824549B2 (en) | High efficiency grit removal system | |
GB2158741A (en) | Separation of components of a fluid mixture | |
CN105836932A (en) | Method for treating wastewater containing sediment | |
US5520806A (en) | Apparatus for gas bubble flotation | |
US20140190897A1 (en) | Enhanced separation of nuisance materials from wastewater | |
Ingersoll et al. | Fundamental concepts of rectangular settling tanks | |
JP3681003B2 (en) | Suspension separation method, suspension separator, sedimentation channel module, suspension separator unit | |
CN108455695A (en) | A kind of impact-resistant efficient air-floating system and its sewage water treatment method | |
US10065197B2 (en) | Hydraulic particle separation apparatus for placer mining | |
KR200220590Y1 (en) | Sewage treatment centrifuge with separation of suspended solids | |
JPS58143860A (en) | Floating separation apparatus | |
Shammas et al. | Sedimentation | |
CN210711079U (en) | Pipeline cleaning sewage treatment device | |
CN108946890A (en) | A kind of sewage disposal system integrating purification with concentration | |
KR102421273B1 (en) | Sedimentation tank for increasing separation efficiency of suspended solids | |
US3721347A (en) | Purification device for removing heavy components from a suspension | |
EP0873278B1 (en) | Method for adding oxygen to water | |
CN106315713B (en) | Integrated girt-water separation device | |
SU946591A1 (en) | Thin film settler | |
CN208413913U (en) | A kind of impact-resistant efficient air-floating system | |
CN211226665U (en) | A sedimentation tank for sewage treatment | |
KR100326914B1 (en) | High speed separator for water & wastewater treatment | |
JPS63182009A (en) | Solid and liquid separator of raw water such as sludge | |
HU181464B (en) | Stripping device for separating contaminations suspended in fluids particularly for ones of smaller specific density than that of fluid advantageously for purifying sewages containing oil | |
CA1168991A (en) | Topological separator |