JP2527334Y2 - Settling tank - Google Patents

Settling tank

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Publication number
JP2527334Y2
JP2527334Y2 JP1989114711U JP11471189U JP2527334Y2 JP 2527334 Y2 JP2527334 Y2 JP 2527334Y2 JP 1989114711 U JP1989114711 U JP 1989114711U JP 11471189 U JP11471189 U JP 11471189U JP 2527334 Y2 JP2527334 Y2 JP 2527334Y2
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Japan
Prior art keywords
sludge
sedimentation tank
mud
cone
collection chamber
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.)
Expired - Lifetime
Application number
JP1989114711U
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Japanese (ja)
Other versions
JPH0356603U (en
Inventor
料 小林
Original Assignee
福永 和二
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Priority to JP1989114711U priority Critical patent/JP2527334Y2/en
Publication of JPH0356603U publication Critical patent/JPH0356603U/ja
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Publication of JP2527334Y2 publication Critical patent/JP2527334Y2/en
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  • Treatment Of Sludge (AREA)
  • Mixers Of The Rotary Stirring Type (AREA)

Description

【考案の詳細な説明】 [産業上の利用分野] 本考案は、沈澱槽の沈降汚泥を中央に集泥機の掻取羽
根(レーキ)で集泥する沈澱槽に係るものであり、集泥
効率を向上するため、沈澱槽底部の勾配(傾斜角度)、
沈澱槽の底部中央に設けた集泥室内の偏芯円錐、偏芯楕
円錐の沈澱汚泥移送装置に関するものである。
[Detailed description of the invention] [Industrial application field] The present invention relates to a sedimentation tank for collecting sludge in a sedimentation tank in the center with a scraping blade (rake) of a sludge collector. In order to improve efficiency, the slope (tilt angle) at the bottom of the settling tank,
The present invention relates to an eccentric cone and an eccentric elliptic cone settling sludge transfer device provided in a collecting chamber provided at the bottom center of a settling tank.

[従来の技術] 従来の大規模の沈澱槽において、沈澱槽の円筒外周壁
から集泥機中心に向かって傾斜する沈澱槽底部の勾配を
大きくとると、中央の水深が大きくなり、沈澱した生物
汚泥は無酸素状態で沈澱槽内に滞留する時間が長く、沈
澱した生物汚泥の一部が死滅し、消化ガスを発生し、ま
たは脱窒素反応による窒素ガス付着により大塊の汚泥
(フロック)が浮上するため、勾配を大きく採れない。
沈澱槽の底部の勾配が小さく、沈澱槽に流入する汚泥濃
度が高いと、沈澱槽中央部はレーキの腕2本をクロスに
設けて移送量を倍増するものが知られているが、汚泥移
送量は十分でない。
[Prior Art] In a conventional large-scale sedimentation tank, if the inclination of the bottom of the sedimentation tank, which is inclined from the cylindrical outer peripheral wall of the sedimentation tank toward the center of the mud collector, is increased, the water depth in the center becomes large, and Sludge stays in the sedimentation tank in an oxygen-free state for a long time, and part of the settled biological sludge is killed, generating digestion gas, or a large mass of sludge (floc) is generated by nitrogen gas adhesion by the denitrification reaction. Because it rises, it cannot take a large gradient.
When the slope at the bottom of the sedimentation tank is small and the concentration of sludge flowing into the sedimentation tank is high, it is known that the transfer amount is doubled by providing two rake arms on a cloth at the center of the sedimentation tank. The quantity is not enough.

中央集泥室の汚泥払い出し口は、底のある垂直な円筒の
円周から払い出しパイプの口が1ないし複数開口してい
る。
The sludge discharge port of the central mud collection chamber has one or more discharge pipe ports opened from the circumference of a vertical cylinder having a bottom.

[考案が解決しょうとする課題] 沈澱槽底面を同心円で6等分した場合を考えてみよ
う、最外周の環状円は第6環状円、その内側の環状円は
第5環状円、その内側の環状円は第4環状円・・・中心
の円は第1環状円と呼称する。攪はん腕の回転によって
各環状円に沈降した汚泥は積み残し無く、混ぜ合わせる
ことなく順次最外周環状円から順次中心に向かって第1
環状円、集泥室に送られるのがよい。そのためには、攪
はん腕の1回転で一つ内側の環状円のレーキの移送する
汚泥量はその外側の環状円の移送汚泥量の1.1〜1.2倍が
望ましい。中心部第1環状円の集泥レーキ(第1の集泥
レーキと呼称する)の移送量は最外周の環状円集泥レー
キの移送量の約1.8〜2.5倍量の汚泥を中心の集泥室の汚
泥払い出し口に移送出来るのが望ましい。この条件を満
たすには第1の集泥レーキの面積は第1と第6のレーキ
が攪はん腕にたいして同じ角度であれば、第1のレーキ
の面積は第6のレーキの2.5倍以上の面積を持ち、しか
も中心への移送距離は第6のレーキの数倍の距離を移送
して、中央に汚泥を集めることが必要である。攪はん腕
1回転の回転距離が第6のレーキに較べて短い第1環状
円のレーキ(数枚)で中央に移送するには、攪はん腕と
第1のレーキとの角度(夾角)は第6環状円のレーキに
比べて小さくしなければならない。このことはレーキの
面と汚泥との滑りを悪くして汚泥を中央に移送すること
が困難になる場合が多く、第1環状円内で汚泥を混練
(捏和)して汚泥密度が高くなり、汚泥が順次外周部か
ら中心に向かってスムースに移送されないために、滞留
時間の長い汚泥塊が第1〜第3環状円内で浮上する問題
点を有していた。また、中央集泥室の入口に到達した汚
泥は、集泥室入口で混練(捏和)して汚泥密度が高くな
り、集泥室の攪はん軸の攪はん腕が回転していても回転
速度が遅いために、圧密された汚泥は腕に付着して回転
し、集泥室内の払い出しポンプの吸い込み口数が少ない
と、集泥室入口から払い出しポンプの吸い込み口まで水
筋ができて短絡移送される問題点があった。
[Problem to be Solved by the Invention] Let us consider a case where the bottom of the settling tank is equally divided into six concentric circles. The outermost circular circle is the sixth circular circle, the inner circular circle is the fifth circular circle, and the inner circular circle is the sixth circular circle. The annular circle is referred to as a fourth annular circle... The center circle is referred to as a first annular circle. The sludge settled in each annular circle by the rotation of the stirring arm is not left behind, and the first sludge is sequentially moved from the outermost annular circle to the center without mixing.
It is good to be sent to an annular circle, mud collection room. For this purpose, it is desirable that the amount of sludge transferred by the rake of the inner annular circle by one rotation of the stirring arm be 1.1 to 1.2 times the amount of sludge transferred by the outer annular circle. The transfer amount of the sludge collection lake (referred to as the first sludge collection lake) of the first annular circle at the center is about 1.8 to 2.5 times the amount of sludge collected at the outermost annular circle collection lake. It is desirable to be able to transfer to the sludge discharge port of the room. In order to satisfy this condition, the area of the first mud rake is at least 2.5 times the area of the sixth rake if the first and sixth rakes are at the same angle to the stirring arm. It is necessary to have a large area and to transport the sludge several times the distance to the center of the sixth rake to collect sludge in the center. In order to transfer to the center with the rake (several pieces) of the first circular circle, in which the rotation distance of the rotation of the stirring arm is shorter than that of the sixth rake, the angle between the stirring arm and the first rake (the included angle) ) Must be smaller than the rake of the sixth annular circle. This often makes it difficult to transfer the sludge to the center due to poor sliding between the rake surface and the sludge, and the sludge density is increased by kneading (kneading) the sludge in the first annular circle. Since the sludge is not smoothly transferred from the outer peripheral portion toward the center, the sludge mass having a long residence time floats in the first to third annular circles. In addition, the sludge that reaches the entrance of the central collection chamber is kneaded (kneaded) at the entrance of the collection chamber to increase the sludge density, and the stirring arm of the stirring shaft of the collection chamber rotates. Because the rotation speed is low, the compacted sludge adheres to the arm and rotates, and if the number of suction pumps in the collection chamber is small, a water streak is formed from the entrance of the collection chamber to the suction port of the discharge pump. There was a problem of short circuit transfer.

本考案は、大型の沈澱槽、濃度の高い汚泥でも確実に
中央集泥室の払い出し口に圧密することなく移送し、中
央払い出し口で回転によって汚泥を均質化する攪はん腕
と中央集泥室を提供する。
The present invention aims to ensure that even large sedimentation tanks and highly concentrated sludge are transported without consolidation to the discharge port of the central sludge collection chamber, and that the sludge arm and the central sludge that homogenize the sludge by rotation at the central discharge port. Provide room.

[課題を解決するための手段] 本考案における沈澱槽は、沈澱槽水面積の1/2以下の
円面積の円周から沈澱槽中心軸に向かって、底部の勾配
が汚泥と槽底部の安息角以上(4〜41度)の角度をも
ち、沈澱汚泥を集泥室に滑り落ちる構造の底部と、レー
キは勾配の異なる底部に沿って回転する構造をもつもの
であり、中央集泥室への汚泥の移送量はレーキの攪はん
により汚泥の中央への滑り落ちにより容易に最外周汚泥
移送量の数倍にも達する。安息角は汚泥の種類、濃度、
沈澱槽の材質、沈澱槽底部の平滑度に支配される。沈澱
槽底部が鉄板、沈澱汚泥濃度が3〜7kg/m3、沈澱槽入り
口の曝気槽の汚泥負荷が0.15kg/kg日以下であれば、安
息角は3〜25度の範囲である。沈澱槽入り口の曝気槽汚
泥負荷が0.25kg/kg日以上であれば、安息角は5〜40度
の範囲である。
[Means for Solving the Problems] The sedimentation tank in the present invention has a sludge bottom slope from the circumference of a circle area not more than half of the sedimentation tank water area toward the center axis of the sedimentation tank. It has an angle of more than 4 to 41 degrees, and the bottom has a structure that slides the settled sludge into the mud collection chamber, and the rake has a structure that rotates along the bottom with a different slope. The sludge transfer amount can easily reach several times the outermost sludge transfer amount due to the sludge sliding down to the center due to the rake agitation. The angle of repose depends on the type of sludge, its concentration,
It is governed by the material of the precipitation tank and the smoothness of the bottom of the precipitation tank. If the bottom of the settling tank is an iron plate, the concentration of the settling sludge is 3 to 7 kg / m 3 , and the sludge load of the aeration tank at the entrance of the settling tank is 0.15 kg / kg day or less, the angle of repose is in the range of 3 to 25 degrees. If the aeration tank sludge load at the entrance of the settling tank is 0.25 kg / kg day or more, the angle of repose is in the range of 5 to 40 degrees.

沈澱槽底部の中央に設けた集泥室は有底円筒形(第3
図)または、有底広口三角コルベン形(第4図)をも
ち、集泥室入り口は安息角以上の傾斜角度をもつ沈澱槽
底部と集泥室側壁とが接する部分において開口してい
る。集泥室入口は比較的大きく開口し、集泥室に滑り落
ちる汚泥を攪はん羽根と回転軸に偏芯して固定した円錐
または楕円錐が回転軸の回転により、集泥室側壁に設け
た汚泥の払い出しポンプの吸い込み口に送り出すように
した構造をもつものである。
The mud collection chamber provided at the center of the bottom of the settling tank has a bottomed cylindrical shape (No. 3).
(Fig. 4) or a wide-opened triangular corvette with a bottom (Fig. 4), and the entrance of the mud collection chamber is open at the portion where the bottom of the sedimentation tank having an inclination angle equal to or greater than the angle of repose contacts the side wall of the mud collection chamber. The entrance of the mud collection chamber is relatively large, and a cone or elliptical cone eccentrically fixed to the stirring blades and the rotating shaft for sludge sliding down into the mud collecting chamber is provided on the side wall of the mud collecting chamber by rotation of the rotating shaft. It has a structure that discharges the sludge to the suction port of the pump.

[作用] 従来の沈澱槽は外周よりレーキで中央に集泥する場
合、中心部に向かうにしたがって移送する汚泥量が増
し、移送距離が外周部より長いにもかかわらず、レーキ
の回転距離が短いために、レーキと攪はん腕との夾角を
小さくして汚泥を中心部に移送する効率を高めようとす
れば、汚泥とレーキの滑りが悪くなり、汚泥を中心部に
移送する効率が低下し、汚泥がこの部分で混練(捏和)
することになる。
[Action] When the conventional sedimentation tank collects sludge from the outer periphery to the center with a rake, the amount of sludge to be transported increases toward the center and the rotation distance of the rake is short despite the transport distance being longer than the outer periphery. Therefore, if the angle between the rake and the stirring arm is reduced to increase the efficiency of transferring sludge to the center, the sludge and rake slip and the efficiency of transferring sludge to the center decreases. And the sludge is kneaded (kneaded) in this area
Will do.

これに対して汚泥移送量が増える沈殿槽水面積の1/2
以内の水面積の沈殿槽底部の傾斜角を、安息角以上にす
ることにより、汚泥がレーキの掻き寄せ作用によらず
に、汚泥が底部を滑り落ちて順次汚泥を簡単に集泥室入
り口に移送することができる。
On the other hand, the amount of sludge transfer increases,
By setting the inclination angle of the bottom of the sedimentation tank within the water area within the angle of repose to be more than the angle of repose, the sludge slides down the bottom without the raking action of the rake. Can be transported.

集泥室入り口の面積は、沈澱槽水面積の1/8〜1/70と
して、集泥室に汚泥が順次滑り込み易くする。
The area of the entrance of the mud collection chamber is set to 1/8 to 1/70 of the area of the sedimentation tank, so that the sludge can easily slide into the mud collection chamber.

集泥室の攪はん羽根は集泥機の回転軸と共通の回転軸
に固定され、回転により汚泥を送る方向に取り付け、集
泥室内の汚泥濃度の均質化を図る。
The stirring blades of the mud collection chamber are fixed to a common rotation shaft with the rotation shaft of the mud collector, and are installed in the direction in which the sludge is sent by rotation to achieve a uniform sludge concentration in the mud collection chamber.

またこの攪はん軸には偏芯円錐または偏芯楕円錐を固
定して設けることにより集泥室内の空隙率が小さくな
り、汚泥の滞留時間が短くなり、偏芯円錐、偏芯楕円錐
の回転により、速やかに汚泥を集泥室側壁に設けた払い
出しポンプの吸い込み口に送り出すことができる。
In addition, by providing an eccentric cone or an eccentric elliptical cone fixed to the stirring shaft, the porosity in the mud collection chamber is reduced, the residence time of the sludge is shortened, and the eccentric cone and the eccentric elliptical cone are formed. Due to the rotation, the sludge can be quickly sent out to the suction port of the delivery pump provided on the side wall of the mud collection chamber.

[実施例] 実施例について図面を参照して説明する。Example An example will be described with reference to the drawings.

第1図〜第5図において、沈澱槽は金属製、コンクリ
ート製とする。その底部は比較的勾配の緩やかな底部
(3)と急勾配の底部(2)とからなり、底部(3)が
緩やかな勾配をもつて円錐状をなした周辺に溢流樋
(9)を有する浅い円筒形または角形の沈殿槽(10)で
中央に原液(給泥という)を送入する給泥筒(8)があ
り、給泥筒から入った汚泥は沈澱し、沈澱した汚泥は攪
はん腕(6)に固定されたレーキ(5)によって底部
(3)にかき集められる。
1 to 5, the sedimentation tank is made of metal or concrete. The bottom is composed of a relatively gentle bottom (3) and a steep bottom (2), and an overflow gutter (9) is provided around the conical bottom (3) with a gentle slope. In a shallow cylindrical or square sedimentation tank (10), there is a sludge pipe (8) for feeding the undiluted solution (referred to as sludge) at the center. Sludge from the sludge pipe settles, and the sludge settles. The rake (5) fixed to the arm (6) collects it at the bottom (3).

急勾配の底部(2)にきた汚泥はレーキの回転により
底部を滑るように下降した汚泥は中央の集泥室(4)入
口に到達する。集泥室入口の面積は沈澱槽水面積の1/8
〜1/70あれば、滑り落ちてくる汚泥を濃縮することなし
に集泥室に受け入れることが出来る。
The sludge coming to the steep bottom (2) slides down the bottom by the rotation of the rake, and the sludge reaches the entrance of the central sludge collection chamber (4). The area of the mud collection room entrance is 1/8 of the area of the sedimentation tank
If it is up to 1/70, the sludge that falls down can be accepted in the mud collection room without being concentrated.

攪はん軸に固定した集泥室攪はん羽根(11)と偏芯し
た円錐(12)の回転により、集泥室に落下した汚泥は濃
縮されず直ちに側壁の払い出しポンプの吸引口(7)に
送り出し排泥される。偏芯円錐、偏芯楕円錐の固定位置
は、頂点と集泥室の底部に平行な円錐底面において楕円
の長直径と円周との交点から攪はん軸までの距離の比率
を1:2〜1:9とし、長直径は集泥室直径に対し0.5〜0.95
とするのが望ましい。
Due to the rotation of the stirring blades (11) fixed to the stirring shaft and the eccentric cone (12), the sludge that has fallen into the collection chamber is not concentrated and the suction port (7) of the delivery pump on the side wall is immediately concentrated. ) And is discharged. The fixed position of the eccentric cone and the eccentric elliptical cone is the ratio of the distance from the intersection of the long diameter of the ellipse and the circumference to the stirring axis on the cone bottom parallel to the vertex and the bottom of the mud collection chamber, 1: 2 ~ 1: 9, long diameter 0.5 ~ 0.95
It is desirable that

[考案の効果] 本考案は上述のとおり構成されているので、次に記載
する効果をあげる。
[Effects of the Invention] Since the present invention is configured as described above, the following effects can be obtained.

請求項1の汚泥の安息角より急勾配をもつ沈澱槽にお
いては、沈澱槽の底部が沈澱槽の水面積の1/2より小さ
い円面積の円周部より集泥機の中心軸に向かって、汚泥
の安息角より急勾配をもっているのでブレーキの回転で
汚泥が底部の急勾配を滑り落ちて順次汚泥を簡単に集泥
室入口に移送することができる。
In the sedimentation tank having a steeper slope than the angle of repose of the sludge according to claim 1, the bottom of the sedimentation tank is directed toward the center axis of the sludge collector from a circumferential part having a circular area smaller than 1/2 of the water area of the sedimentation tank. Since the sludge has a steep slope than the angle of repose, the sludge can slide down the steep slope at the bottom by the rotation of the brake, and the sludge can be easily transferred to the entrance of the sludge collecting chamber.

請求項2の汚泥を偏芯円錐、偏芯楕円錐底面の楕円の
長直径が集泥室直径の0.5〜0.95とすれば、集泥室内の
汚泥滞留時間が短くなり、汚泥濃度を高めることがなく
なる。
When the sludge of claim 2 has an eccentric cone and an elliptic long diameter of the eccentric elliptical cone bottom of 0.5 to 0.95 of the diameter of the sludge collection chamber, the sludge retention time in the sludge collection chamber is shortened, and the sludge concentration can be increased. Disappears.

底面の攪はん軸固定位置が、楕円長直径と円周との交
点から攪はん軸までの距離の比率が1:2〜1:9とすること
で、回転することにより、降下してくる汚泥を順次集泥
室側壁に開口する払い出しポンプの吸い込み口に確実に
送り込むことができる。
The stirring shaft fixed position on the bottom is lowered by rotating by setting the ratio of the distance from the intersection of the elliptical long diameter and the circumference to the stirring shaft to 1: 2 to 1: 9. Incoming sludge can be reliably sent to the suction port of the dispensing pump that sequentially opens on the side wall of the mud collection chamber.

【図面の簡単な説明】[Brief description of the drawings]

第1図は沈澱槽の縦断面図、第2図は沈澱槽の横断面
図、第3図は有底円筒形集泥室要部の断面図、第4図は
有底広口三角コルベン形集泥室要部の断面図、第5図は
偏芯円錐、偏芯楕円錐底面の攪はん軸の固定位置図、 1……沈澱槽、2……急傾斜底部、3……底部、4……
集泥室、5……レーキ、6……攪はん腕、7……払い出
し(ポンプ)吸い込み口、8……汚泥供給筒、9……溢
流堰、10……沈殿槽、11……攪はん羽根、12……偏芯円
錐(偏芯楕円錐)、13……攪はん軸
1 is a longitudinal sectional view of a sedimentation tank, FIG. 2 is a transverse sectional view of the sedimentation tank, FIG. 3 is a sectional view of a main part of a cylindrical collecting mud chamber having a bottom, and FIG. Sectional view of the main part of the mud chamber, Fig. 5 shows the fixed position of the stirring shaft on the bottom of the eccentric cone and eccentric elliptic cone, 1 ... sedimentation tank, 2 ... steep bottom, 3 ... bottom, 4 ......
Sludge collection chamber, 5 rake, 6 stirring arm, 7 discharge (pump) suction port, 8 sludge supply cylinder, 9 overflow weir, 10 sedimentation tank, 11 Stirring blades, 12: Eccentric cone (eccentric elliptic cone), 13: Stirring axis

Claims (2)

(57)【実用新案登録請求の範囲】(57) [Scope of request for utility model registration] 【請求項1】集泥機が円運動する沈澱槽において、沈澱
槽底部は比較的勾配の緩やかな底部(3)に、沈澱槽水
面積の1/2より小さい円(集泥機中心軸を中心とする)
面積の円周部より、集泥機の中心軸に向って4〜41度の
急勾配をもつ急傾斜底部(2)が接合し、急傾斜底部と
集泥室(4)側壁とが接する部分において開口し、集泥
機のレーキは勾配の異なる底部に沿って回転する構造を
もつ沈澱槽。
In a sedimentation tank in which a sludge collector moves in a circle, the bottom of the sedimentation tank has a relatively gentle slope (3), and a circle smaller than half the water area of the sedimentation tank. Center)
From the circumference of the area, the steep bottom (2) having a steep slope of 4 to 41 degrees toward the central axis of the mud collector is joined, and the steep bottom and the side wall of the mud collection chamber (4) are in contact. The sedimentation tank has a structure that opens at and the rake of the mud collector rotates along the bottom with different slopes.
【請求項2】集泥室内に集泥機の回転軸を攪はん軸と
し、その軸に固定された偏芯円錐、偏芯楕円錐を有し、
かつその固定位置は、円錐または楕円錐の頂点と底面に
おいて楕円の長直径と円周との交点から攪はん軸までの
距離の比率を1:2〜1:9の範囲に、また長直径は集泥室直
径に対し0.5〜0.95の範囲とした沈殿汚泥移送装置を有
する請求項1)に記載の沈殿槽。
2. A mud collecting chamber, wherein a rotating shaft of the mud collector is used as a stirring shaft, and an eccentric cone and an eccentric elliptical cone fixed to the shaft are provided.
The fixed position is the ratio of the distance from the intersection of the major axis of the ellipse to the circumference at the apex and base of the cone or elliptical cone to the stirring axis within the range of 1: 2 to 1: 9, The sedimentation tank according to claim 1, further comprising a settling sludge transfer device having a range of 0.5 to 0.95 with respect to the diameter of the collection chamber.
JP1989114711U 1989-09-29 1989-09-29 Settling tank Expired - Lifetime JP2527334Y2 (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
JP1989114711U JP2527334Y2 (en) 1989-09-29 1989-09-29 Settling tank

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
JP1989114711U JP2527334Y2 (en) 1989-09-29 1989-09-29 Settling tank

Publications (2)

Publication Number Publication Date
JPH0356603U JPH0356603U (en) 1991-05-30
JP2527334Y2 true JP2527334Y2 (en) 1997-02-26

Family

ID=31663064

Family Applications (1)

Application Number Title Priority Date Filing Date
JP1989114711U Expired - Lifetime JP2527334Y2 (en) 1989-09-29 1989-09-29 Settling tank

Country Status (1)

Country Link
JP (1) JP2527334Y2 (en)

Families Citing this family (1)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
ITPN20110039A1 (en) * 2011-05-24 2012-11-25 Keyline S P A GRIPPING BLOCK PERFECTED FOR DUPLICATING KEY MACHINE

Family Cites Families (4)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JPS5019055A (en) * 1973-06-20 1975-02-28
US4000075A (en) * 1975-12-31 1976-12-28 Dorr-Oliver Incorporated Sedimentation tank with rotary yieldable rake arm structure
JPS6036837B2 (en) * 1977-07-08 1985-08-22 株式会社クボタ Sewage purification equipment
JPS60122012A (en) * 1983-12-02 1985-06-29 Mitsubishi Heavy Ind Ltd Sludge collecting apparatus

Also Published As

Publication number Publication date
JPH0356603U (en) 1991-05-30

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