JPS58112007A - Separation of solid substance contained in water - Google Patents

Separation of solid substance contained in water

Info

Publication number
JPS58112007A
JPS58112007A JP21554481A JP21554481A JPS58112007A JP S58112007 A JPS58112007 A JP S58112007A JP 21554481 A JP21554481 A JP 21554481A JP 21554481 A JP21554481 A JP 21554481A JP S58112007 A JPS58112007 A JP S58112007A
Authority
JP
Japan
Prior art keywords
water
inclined plate
separation chamber
solids
solid substance
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
Application number
JP21554481A
Other languages
Japanese (ja)
Inventor
Mitsugi Miura
貢 三浦
Current Assignee (The listed assignees may be inaccurate. Google has not performed a legal analysis and makes no representation or warranty as to the accuracy of the list.)
Miura Engineering International Co Ltd
Original Assignee
Miura Engineering International Co Ltd
Priority date (The priority date 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 date listed.)
Filing date
Publication date
Application filed by Miura Engineering International Co Ltd filed Critical Miura Engineering International Co Ltd
Priority to JP21554481A priority Critical patent/JPS58112007A/en
Publication of JPS58112007A publication Critical patent/JPS58112007A/en
Pending legal-status Critical Current

Links

Abstract

PURPOSE:To eliminate the obstraction of the slide-down of a precipitate due to an obliquely rising stream, by precipitating solid substance on the surface of a perforated inclined plate when water containing said solid substance rises obliquely and falling the same into a separation chamber to eliminate the re-entry of the precipitate into water. CONSTITUTION:When water containing solid substance sent into from a raw water inlet 5 rises obliquely through a gap 7, the solid substance is precipitated onto the surface of a perforated inclined plate 2 and enters a separation chamber 10 from orifices 8. The upper end of the separation chamber is closed by a closing plate 4 and water is not flowed upwardly. Water is obliquely raised to be flowed into a treating tank 9 and discharged from a discharge pipe 21. The solid substance is transferred to the bottom 11 of the separation chamber 10 and transferred to a thickener bottom 15 through a falling pipe 14 from an opening part 13 to be discharged through a valve 16. Plural falling pipes 14 are studded in a bottom part 6 but, because gaps are mutually provided between pipes, raw water is extended throughout the cross area of the tank bottom part and is obliquely raised through all gaps 7 between separation chambers 10 to carry out solid substance precipitating and separating work. Raw water rising from the tank bottom part is not collided with the precipitate solid down toward the lower end of the inclined plate.

Description

【発明の詳細な説明】 従来、液体中の固形物を沈澱分離したり、排水処理で凝
集フロックを沈澱分離するのに傾斜板型シックナーが広
く採用されている。この原理は第1図に示す如く固形物
や凝集フロック(以下固形物と総称する)を含む液体や
水(以下水と総称する)が傾斜板間を斜上昇流する時、
固形物が水の斜上昇流に打勝って傾斜板上に沈澱し、沈
澱物が傾斜板面上を滑り落ち傾斜板下端より槽底に落ち
、一方固形物を分離した清澄水が槽頂より排出する方法
である。
DETAILED DESCRIPTION OF THE INVENTION Hitherto, inclined plate thickeners have been widely used to separate solids in liquids by sedimentation or to separate flocs in wastewater treatment by sedimentation. This principle is as shown in Fig. 1, when liquid or water (hereinafter collectively referred to as water) containing solids and flocs (hereinafter collectively referred to as solids) flows obliquely upward between inclined plates.
The solids overcome the upward flow of water and settle on the sloped plate, and the precipitates slide down the sloped plate surface and fall to the bottom of the tank from the bottom of the sloped plate, while the clear water from which the solids have been separated flows from the top of the tank. This is a method of discharging it.

この方法には下記の欠点がある。This method has the following drawbacks.

第一の欠点は傾斜板面上に沈澱した固形物の表面を水が
斜上昇するから、沈澱固形物の傾斜板面へ下方への滑り
落ちを防害し、水の斜上昇速度が速い時は一旦沈澱した
固形物の一部を水中に還元し再び斜上昇略せることであ
る。
The first drawback is that the water rises obliquely on the surface of the solids precipitated on the inclined plate surface, so it is necessary to prevent the precipitated solids from sliding downward onto the inclined plate surface, and when the water rises at a high speed, Part of the solids that have settled once are returned to the water and the sloping rise again can be omitted.

第二の欠点は、傾斜面上を滑り落ちた固形物が。The second drawback is that solid objects slide down the slope.

傾斜板最下端から槽底に流下する時、槽底部から上昇す
る原水と衝突し、固形物の沈降が妨害され最悪の場合は
沈澱物の一部が再び原水に混って上昇することである。
When flowing down from the bottom of the inclined plate to the bottom of the tank, it collides with the raw water rising from the bottom of the tank, preventing the solids from settling, and in the worst case, some of the sediment will mix with the raw water and rise again. .

本発明は、上記の欠点を無くする傾斜板型シックナーの
方法と装置であり、第2図にて説明する。
The present invention is a method and apparatus for a tilted plate thickener that eliminates the above drawbacks and is illustrated in FIG.

傾斜板型シックナー(1)の中に、無孔傾斜板(2)と
有孔傾斜板(3)を上端の封鎖板(4)で封鎖してなる
単位分離器を複数組格納させである。
A plurality of unit separators each consisting of a non-perforated inclined plate (2) and a perforated inclined plate (3) sealed by a sealing plate (4) at the upper end are stored in an inclined plate type thickener (1).

原水入口(5)より送入される固形物を含む原水が分離
−相互間の間隙(7)を斜上昇する時、固形物は有孔傾
斜面上に沈澱し、次かで沈澱物は孔(8)を通シ両傾斜
板で構成される分離室(10)に入る。分離室の上端は
封鎖板(4)で閉鎖されているから分離室内では水の上
昇流が無く或は殆んど無く、分離室に入った固形物は原
水上昇流による影響を全く或゛は殆んど受けずに無孔傾
斜板面に沈澱し、沈澱した固形物は無孔傾斜板面を4り
落・ちる。一方固形物を分離した水は一ヒ端の処理水槽
(9)へ斜上昇した後清澄水排出管(21)より排出さ
れる。
When the raw water containing solids introduced from the raw water inlet (5) ascends obliquely through the separation gap (7), the solids settle on the perforated inclined surface, and then the precipitates pass through the pores. (8) Enter the separation chamber (10) consisting of two inclined plates. Since the upper end of the separation chamber is closed with a sealing plate (4), there is no or almost no upward flow of water in the separation chamber, and the solids that enter the separation chamber are not affected by the upward flow of raw water at all. It precipitates on the non-porous inclined plate surface with almost no reception, and the precipitated solids fall down the non-porous inclined plate surface. On the other hand, the water from which the solids have been separated rises obliquely to the treated water tank (9) at one end and is then discharged from the clear water discharge pipe (21).

無孔傾斜板面を滑り落ちた固形物は第3図でその断面を
示す分離室底(11)に移る。分離室底(11)は底板
部(工2)と開孔部(13)が交互に存在し、固形物は
開孔部(13)より固形物沈降管(14)を通りシック
ナー底(15)に移り排出弁(16)を通じて排出され
る。シックナ一槽底部(6)は多数の固形物沈降管(1
4)が点在しているが、固形物沈降管相互間には空隙部
がある為、原水管(5)より送入された原水は槽底部所
面に行きわたり、原水は全ての分離器相互管の間隙(7
)より斜上昇流して固形物沈澱分離作業が行なわれる。
The solid matter that has slipped down the non-porous inclined plate surface moves to the bottom (11) of the separation chamber, the cross section of which is shown in FIG. The bottom of the separation chamber (11) has a bottom plate part (work 2) and an opening part (13) alternately, and the solids pass through the opening part (13) and the solid settling tube (14) to the thickener bottom (15). and is discharged through the discharge valve (16). The bottom of the thickener tank (6) has a large number of solid sedimentation tubes (1
4) are scattered, but since there are gaps between the solid settling pipes, the raw water sent from the raw water pipe (5) is distributed all over the bottom of the tank, and the raw water flows through all the separators. Interpipe gap (7
), the solids are precipitated and separated.

上述で明らかな如く、本発明は固形物を含む水が傾上昇
する時、固形物が有孔傾斜板面に沈澱し引続き孔より分
離室に落下するから、従来の傾斜板型シックナーの場合
の沈澱物の水中への還元が無く、分離室に入り無孔傾斜
板面上に沈澱した沈澱物は従来の傾斜板シックナーの場
合の水の斜上昇流による沈澱物の滑り落ちの妨害がない
As is clear from the above, the present invention is advantageous in that when water containing solids is tilted upward, the solids settle on the perforated inclined plate surface and subsequently fall into the separation chamber through the holes, which is different from the case of the conventional inclined plate type thickener. There is no return of the precipitate into water, and the precipitate that enters the separation chamber and settles on the non-porous inclined plate surface is not prevented from sliding down due to the oblique upward flow of water in the case of the conventional inclined plate thickener.

さらに、傾斜板下端へ滑り落ちた沈澱物は管を通りシッ
クナー底へ落下するから、従来の傾斜板シックナーの場
合の如く、一槽底部から上昇する原水との衝突が無く固
形物の沈降妨害や原料水への混入が無い等多くの優れた
特長がある。
Furthermore, since the sediment that has slipped to the lower end of the inclined plate passes through the pipe and falls to the bottom of the thickener, there is no collision with the raw water rising from the bottom of the tank, unlike in the case of conventional inclined plate thickeners, and there is no interference with settling of solids. It has many excellent features such as no contamination with raw water.

上述で本発明方法を説明したが、その装置化には種々の
応用や変化がある。例えば、上述では固形物沈降管(1
4)の下端がシックナー底(15)へ開放しているが、
下端を直接槽外へ解放してもよい。
Although the method of the present invention has been described above, there are various applications and variations in its implementation. For example, in the above example, the solid settling tube (1
4) The lower end is open to the thickener bottom (15),
The lower end may be directly released to the outside of the tank.

設備費を安くするため、発明者が願書番号昭52−(>
04644で特許申請した1−傾斜板型沈降装置」に特
許出願した金属板の代りに繊維、プラスチックのフィル
ム、ゴム等の膜を使用する単一分離器を使用してもよい
In order to reduce equipment costs, the inventor filed an application with application number 1972-(>
A single separator using a membrane made of fiber, plastic film, rubber, etc. may be used instead of the metal plate, which was applied for patent in 1-Incline Plate Sedimentation Apparatus, filed under No. 04644.

第4図に示す如く上方に孔が無く下方に孔のある長いフ
ィルムの両端に金属棒(16)をとりつけ、第5図の如
くフィルム中央部を有孔部を上面にして二本の棒(17
) 、 (18)に架け、フィルムの下方部に二本の棒
(19) 、 (2o)に架けると、金属棒(16)の
重量により有孔膜と無孔膜が緊張状体に懸垂するので極
めて安価な単位分離器が得られる。
As shown in Figure 4, metal rods (16) are attached to both ends of a long film that has no holes at the top and holes at the bottom, and two rods (16) are attached to the central part of the film with the perforated part facing upward as shown in Figure 5. 17
), (18) and two rods (19), (2o) below the film, the weight of the metal rod (16) causes the perforated membrane and non-porous membrane to suspend in a tension-like body. Therefore, an extremely inexpensive unit separator can be obtained.

【図面の簡単な説明】[Brief explanation of the drawing]

第1図は従”来の傾斜板シックナーの構造、第2図第2
′図は本発明のシックナーの構造、第3図は分離室底の
断面図、第4図、第5図は金属板の代シにフィルムを使
用した単位分離器を示す。 (2)・・・無孔傾斜板       (8)・・・孔
(3)・・・有孔傾斜板      (10)・・・分
離室(4)・・・封鎖板        (12)・・
・底板部(7)・・・分離器相互間の間隙  (13)
・・・開孔部(14)・・・沈降管 出願人  ミウラエンジニャリングインターナショナル
株式会社取締役社長  三 浦   貢 手  続  補  正  書 昭和57年を月〕/日 1、事件の表示 昭和56年特許願第215544号 2、発明の名称 水中に含有される固形物の分離方法 3、補正をする者 事件との関係  特許出願人本人 昭和57年4月27日 5、補正の対象 明細書の「図面の簡単な説明」と図面 間     細     書 16  発明の名称 水中に含有される固形物の分離方法 2、特許請求の範囲 (1)本文に詳述した如く、上方が有孔、下方が無孔の
2枚の傾斜板を一定の間隔をおき並列させ、双方の上端
に封鎖板を設けたものを単位分離器とし、この単位分離
器を間隔をおいて多数並列させた傾斜板型シックナーに
て、単位分離器相互間に固体を含む水を斜上昇させ、有
孔傾斜板面に沈澱した固形物が孔を通り有孔と無孔の傾
斜板が形成する分離室に入り、次いで下方に沈降させ、
固形物を分離した水を傾斜板上方より清澄水として排出
させることを特長とする水中に含有される固形物の分離
方法。 (2) られた沈降管により、槽底へ降下させることを特長とす
る水中に含有される固形物の分離方法。 3、発明の詳細な説明 従来、液体中の固形物を沈澱分離したり、排水処理で凝
集70ツクを沈澱分離するのに傾斜板型シックナーが広
く採用されている。この原理は第1図に示す如く固形物
や凝集フロック(以下固形物と総称する)を含む液体や
水(以下水と総称する)が傾斜板(22)間を斜上昇流
する時、固形物が水の斜上昇流に打勝って傾斜板(22
)上に沈澱し、沈澱物が傾斜板面上を滑り落ち傾斜板下
端より槽底(23)に落ち、一方固形物を分離した清澄
水が槽頂(21)より排出する方法である。 この方法には下記の欠点がある。 第一の欠点は傾斜板面上に沈澱した固形物の表面を水が
斜上昇するから、沈澱固形物の傾斜板面へ下方への滑シ
落ちを防害し、水の斜上昇速度が速い時は一旦沈澱した
固形−の一部を水中に還元し再び斜上昇させることであ
る。 第二の欠点は、傾斜面上を滑り落ちた固形物が、傾斜板
最下端から槽底に流下する時、槽底部から上昇する原水
と衝突し、固形物の沈降が妨害され最悪の場合は沈澱物
の一部が再び原水に混って上昇することである。 本発明は、上記の欠点を無くする傾斜板型シックナーに
よる水中の含有物の分離方法であり、第2図とその側面
図の第3図にて説明する。 傾斜板型シックナー(υの中に、無孔傾斜板(2)と有
孔傾斜板(3)を上端の封鎖板(4)で封鎖してなる単
位分離器を複数組格納させである。 原水入口(5)より送入される固形物を含む原水が分離
器相互管の間隙(7)を斜上昇する時、固形物は有孔傾
斜面上に沈澱し、次いで沈澱物は孔(8)を通り両傾斜
板で構成される分離室(10)に入る。分離室の上端は
封鎖板(4)で閉鎖されているから分離室内では水の上
昇流が無く或は殆んど無く、分離室に入った固形物は原
水上昇流による影響を全く或は殆んど受けず:’c′舞
孔傾斜孔傾斜板面澱′し、沈澱した固形物は無孔傾斜板
面を滑シ落ちる。一方固形物を分離した水は上端の処理
水槽(9)へ斜上昇しだ後清澄水排出管(21)より排
出される。 無孔傾斜板面を滑り落ちた固形物は第4図でその断面を
示す分離室底(11)に移る。分離室底(11)は底板
部(12)と開孔部(13)が交互に存在し、固形物は
開孔部(13)より固形物沈降管(14)を通りシック
ナー底(15)に移り排出弁(16)を通じて排出され
る。シックナ一槽底部(6)ハ多数の固形物沈降管(1
4)が点在しているが、固形物沈降管相互間には空隙部
がある為、原水管(5)より送入された原水は槽底部断
面に行きわたり、原水は全ての分離器相互管の間隙(7
)より斜上昇流して固形物沈澱分離作業が行なわれる。 上述で明らかな如く、本発明は固形物を含む水が傾上昇
する時、固形物が有孔傾斜板面に沈澱し引続き孔より分
離室に落下するから、従来の傾斜板型シックナーの場合
の沈澱物の水中への還元が無く、分離室に入り無孔傾斜
板面上に沈澱した沈澱物は従来の傾斜板シックナーの場
合の水の斜上昇流による沈澱物の滑シ落ちの妨害がない
・さらに、傾斜板下端へ滑り落ちた沈澱物は管を通シシ
ックナー底へ落下するから、従来の傾斜板シックナーの
場合の如く、槽底部から上昇する原水との衝突が無く固
形物の沈降妨害や原料水への混入が無い等多くの優れた
特長があるO上述で本発明方法を説明したが、その装置
化には種々の応用や変化がある。例えば、上述では固形
物沈降管(14)の下端が7ソクナー底(15)へ開放
しているが、下端を直接槽外へ解放してもよいO設備費
を安くするため、発明者が願書番号昭52−00464
4で特許申請した「傾斜板型沈降装置」に特許出願した
如く金属板の代りに繊維、プラスチックのフィルム、ゴ
ム等の膜を使用する単一分離器を使用してもよい0 第5図に示す如く上半に孔が無く下半に孔のある長いフ
ィルムの両端に金属棒(16) ’eとりつけ、第6図
の如くフィルム中央部を有孔部を上面にして二本の棒(
17) 、 (18)に架け、フィルムの下方部に二本
の棒(19) 、 (20)に架けると、金属棒(16
)の重量により有孔膜と無孔膜が緊張状態に懸垂するの
で極めて安価な単位分離器が得られる。 4、図面の簡単な説明 第1図は従来の傾斜板7ツクナーの構造、第2図第3図
は本発明のシックナーの構造、第4図は分離室底の断面
図、第5図、第6図は金属板の代りにフィルムを使用し
た単位分離器を示す。 (2)・・・無孔傾斜板      (8)・・・孔(
3)・・・有孔傾斜板     (10)・・・分離室
(4)・・・封鎖板       (12)・・・底板
部(7)・・・分離器相互間の間隙  (I3)・・・
開孔部(14)・・・沈降管 出願人  ミウラエンジニャリングインターナショナル
株式会社取締役社長 三 浦   貢
Figure 1 shows the structure of a conventional inclined plate thickener, Figure 2
Figure '' shows the structure of the thickener of the present invention, Figure 3 is a sectional view of the bottom of the separation chamber, and Figures 4 and 5 show a unit separator using a film instead of a metal plate. (2)... Non-perforated inclined plate (8)... Hole (3)... Perforated inclined plate (10)... Separation chamber (4)... Separation plate (12)...
・Bottom plate part (7)...Gap between separators (13)
...Aperture (14) ...Settlement tube applicant Miura Engineering International Co., Ltd. President and CEO Mitsugu Miura Proceedings Amendment Document 1982 (Monday) / Day 1, Incident Indication 1982 Patent Application No. 215544 2, Name of the invention Method for separating solids contained in water 3, Relationship with the case by the person making the amendment Patent applicant April 27, 1981 5, “Drawings” of the specification to be amended 16 Name of the invention Method for separating solids contained in water 2, Claims (1) As detailed in the main text, the upper part is perforated and the lower part is non-porous. A unit separator is a unit separator in which two inclined plates are arranged in parallel at a certain interval and a sealing plate is provided at the upper end of both sides. Water containing solids is allowed to rise between the unit separators at an angle, and the solids that have settled on the perforated inclined plate surface pass through the holes and enter the separation chamber formed by the perforated and non-perforated inclined plates, and are then allowed to settle downward. ,
A method for separating solids contained in water, characterized by discharging water from which solids have been separated as clear water from above an inclined plate. (2) A method for separating solids contained in water, which is characterized by lowering solids to the bottom of a tank using a sedimentation tube. 3. Detailed Description of the Invention Hitherto, inclined plate thickeners have been widely used to separate solids in liquids by sedimentation or to separate aggregates in wastewater treatment by sedimentation. This principle is as shown in Figure 1, when liquid or water (hereinafter collectively referred to as water) containing solids and flocs (hereinafter collectively referred to as solids) flows obliquely upward between the inclined plates (22), the solids The slanted plate (22
), the precipitate slides down on the inclined plate surface and falls from the lower end of the inclined plate to the tank bottom (23), while the clear water from which the solids have been separated is discharged from the tank top (21). This method has the following drawbacks. The first drawback is that water rises obliquely on the surface of the solids precipitated on the inclined plate surface, so it is necessary to prevent the precipitated solids from sliding downward onto the inclined plate surface, and when the water rises obliquely at a high speed. The process involves returning part of the solids that have settled into the water and raising them up again. The second drawback is that when the solids that have slid down the slope descend from the bottom of the slope to the bottom of the tank, they collide with the raw water rising from the bottom of the tank, preventing the solids from settling, and in the worst case scenario. Part of the sediment mixes with the raw water again and rises. The present invention is a method for separating substances contained in water using an inclined plate thickener that eliminates the above-mentioned drawbacks, and will be explained with reference to FIG. 2 and FIG. 3, which is a side view thereof. A plurality of unit separators each consisting of a non-perforated inclined plate (2) and a perforated inclined plate (3) sealed with a sealing plate (4) at the upper end are stored in an inclined plate type thickener (υ). Raw water When the raw water containing solids fed through the inlet (5) ascends obliquely through the gap (7) between the separator tubes, the solids precipitate on the perforated inclined surface, and then the precipitates pass through the holes (8). The upper end of the separation chamber is closed with a sealing plate (4), so there is no or almost no upward flow of water in the separation chamber, and the separation is completed. The solids that enter the chamber are not affected by the upward flow of raw water at all or are hardly affected by the upward flow of raw water: they settle on the inclined plate surface of the inclined hole and the precipitated solids slide down the non-porous inclined plate surface. On the other hand, the water from which the solids have been separated begins to ascend obliquely to the treated water tank (9) at the upper end and is then discharged from the clear water discharge pipe (21). Moving on to the separation chamber bottom (11), which shows the cross section of the separation chamber, the separation chamber bottom (11) has a bottom plate portion (12) and an opening portion (13) alternately existing, and the solids are more solid than the opening portion (13). The solids pass through the settling pipe (14) to the thickener bottom (15) and are discharged through the discharge valve (16).
4) are scattered, but since there are voids between the solid settling pipes, the raw water sent from the raw water pipe (5) is distributed across the bottom section of the tank, and the raw water flows between all the separators. Pipe gap (7
), the solids are precipitated and separated. As is clear from the above, the present invention is advantageous in that when water containing solids is tilted upward, the solids settle on the perforated inclined plate surface and subsequently fall into the separation chamber through the holes, which is different from the case of the conventional inclined plate type thickener. There is no return of the precipitate into water, and the precipitate that enters the separation chamber and settles on the surface of the non-porous inclined plate does not prevent the precipitate from sliding off due to the oblique upward flow of water in the case of conventional inclined plate thickeners.・Furthermore, since the sediment that has slipped to the bottom of the inclined plate falls through the pipe to the bottom of the tank, there is no collision with the raw water rising from the bottom of the tank, which is the case with conventional inclined plate thickeners, and there is no interference with settling of solids. Although the method of the present invention has been described above, there are various applications and variations in its apparatus. For example, in the above example, the lower end of the solid sedimentation tube (14) is open to the bottom of the 7-sockener (15). Number Showa 52-00464
A single separator that uses a membrane made of fiber, plastic film, rubber, etc. instead of a metal plate may be used instead of a metal plate, as in the case of the patent application for the ``inclined plate sedimentation device'' applied for in Figure 4. Attach metal rods (16)'e to both ends of a long film that has no holes in the upper half and holes in the lower half as shown, and attach two rods (16) to the central part of the film with the perforated part facing up as shown in Figure 6.
17) and (18), and two rods (19) and (20) below the film, the metal rod (16)
), the perforated membrane and the non-porous membrane are suspended under tension, resulting in an extremely inexpensive unit separator. 4. Brief description of the drawings Figure 1 shows the structure of a conventional thickener with 7 inclined plates. Figure 6 shows a unit separator using a film instead of a metal plate. (2)... Non-perforated inclined plate (8)... Hole (
3)...Perforated inclined plate (10)...Separation chamber (4)...Blocking plate (12)...Bottom plate (7)...Gap between separators (I3)...・
Opening part (14)...Settlement tube applicant Mitsugu Miura, President and Director of Miura Engineering International Co., Ltd.

Claims (2)

【特許請求の範囲】[Claims] (1)本文に詳述した如く、上方が有孔、下方が無孔の
2枚の傾斜板を一定の間隔をおき並列させ、双方の上端
に封鎖板を設けたものを単位分離器とし、この単位分離
器を間隔をおいて多数並列させた傾斜板型シックナーに
て、単位分離器相互間に固体を含む水を斜上昇させ、有
孔傾斜板面に沈澱した固形物が孔を通り有孔と無孔の傾
斜板が形成する分離室に入り、次いで下方に沈降させ、
固形物を分離した水を傾斜板上方より清澄水として排出
させることを特長とする水中に含有される固形物の分離
方法。
(1) As detailed in the main text, a unit separator is a unit separator in which two inclined plates with holes on the upper side and non-perforated on the lower side are arranged in parallel at a certain interval, and sealing plates are provided at the upper ends of both; In an inclined plate type thickener in which a large number of unit separators are arranged in parallel at intervals, water containing solids is allowed to rise obliquely between the unit separators, and the solids precipitated on the perforated inclined plate surface pass through the holes. into a separation chamber formed by perforated and imperforate inclined plates, and then allowed to settle downward;
A method for separating solids contained in water, characterized by discharging water from which solids have been separated as clear water from above an inclined plate.
(2)特許請求範囲(1)を実施するに於て、分離室底
に滑り落ちた沈澱物を分離室底断面一部に設けられた沈
降管により、槽底へ降下させることを特長とする水中に
含有される固形物の分離方法。
(2) In carrying out claim (1), the feature is that the sediment that has slipped to the bottom of the separation chamber is lowered to the bottom of the tank by a sedimentation pipe provided in a part of the cross section of the bottom of the separation chamber. A method for separating solids contained in water.
JP21554481A 1981-12-24 1981-12-24 Separation of solid substance contained in water Pending JPS58112007A (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
JP21554481A JPS58112007A (en) 1981-12-24 1981-12-24 Separation of solid substance contained in water

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
JP21554481A JPS58112007A (en) 1981-12-24 1981-12-24 Separation of solid substance contained in water

Publications (1)

Publication Number Publication Date
JPS58112007A true JPS58112007A (en) 1983-07-04

Family

ID=16674180

Family Applications (1)

Application Number Title Priority Date Filing Date
JP21554481A Pending JPS58112007A (en) 1981-12-24 1981-12-24 Separation of solid substance contained in water

Country Status (1)

Country Link
JP (1) JPS58112007A (en)

Cited By (2)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JPS58141704U (en) * 1982-03-16 1983-09-24 清水建設株式会社 Sedimentation tank
JP2013043140A (en) * 2011-08-25 2013-03-04 Institute Of National Colleges Of Technology Japan Inclined separation device and separation method using the inclined separation device

Cited By (3)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JPS58141704U (en) * 1982-03-16 1983-09-24 清水建設株式会社 Sedimentation tank
JPS6227202Y2 (en) * 1982-03-16 1987-07-13
JP2013043140A (en) * 2011-08-25 2013-03-04 Institute Of National Colleges Of Technology Japan Inclined separation device and separation method using the inclined separation device

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