JPH0445803A - Sludge removing device - Google Patents

Sludge removing device

Info

Publication number
JPH0445803A
JPH0445803A JP15400990A JP15400990A JPH0445803A JP H0445803 A JPH0445803 A JP H0445803A JP 15400990 A JP15400990 A JP 15400990A JP 15400990 A JP15400990 A JP 15400990A JP H0445803 A JPH0445803 A JP H0445803A
Authority
JP
Japan
Prior art keywords
sludge
valve
tank
pipe
stem
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
Application number
JP15400990A
Other languages
Japanese (ja)
Other versions
JPH0647043B2 (en
Inventor
Masayuki Kawame
川目 正幸
Hideo Nakayama
秀夫 中山
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.)
Honda Motor Co Ltd
Parker Netsushori Kogyo KK
Original Assignee
Honda Motor Co Ltd
Parker Netsushori Kogyo KK
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 Honda Motor Co Ltd, Parker Netsushori Kogyo KK filed Critical Honda Motor Co Ltd
Priority to JP2154009A priority Critical patent/JPH0647043B2/en
Publication of JPH0445803A publication Critical patent/JPH0445803A/en
Publication of JPH0647043B2 publication Critical patent/JPH0647043B2/en
Anticipated expiration legal-status Critical
Expired - Lifetime legal-status Critical Current

Links

Abstract

PURPOSE:To efficiently separate and remove sludge by providing an upper chamber having an inverted conical bottom with its inlet pipe opened at a position away from the center, a flow straightening pipe, a shell in which sludge is settled, a hopper forming the bottom of a removal tank, valves, a discharge pump and a lid. CONSTITUTION:A sludge-contg. liq. is supplied to the upper chamber 3 of a removal tank 1 from an inlet pipe 10, settled and allowed to flow down into a shell 5 through a flow straightening pipe 4. The fluid with the ascending speed reduced in the shell 5 is returned to a treating tank through an outlet pipe 11. The sludge is settled in this process, deposited in a hopper 6 and concentrated. The sludge is discharged into a sludge pan 17 by operating a valve 7 with a handle 9. The liq. temp. in the tank 1 and the temp. of the contact part of the outlet pipe 11 with the atmosphere are kept constant by a heating and temp. control means, and the pipe 10 is covered with an insulating material and kept warm. A liq. level gage having a detection alarm for the liq. level is furnished to the tank 1.

Description

【発明の詳細な説明】 〔産業上の利用分野〕 本発明は各種処理装置に併設され、処理装置の液体中に
浮遊混入するスラッジを除去するスラッジ除去装置に関
する。
DETAILED DESCRIPTION OF THE INVENTION [Field of Industrial Application] The present invention relates to a sludge removal device that is attached to various processing devices and removes sludge floating in the liquid of the processing device.

〔従来の技術〕[Conventional technology]

溶融塩、水溶液もしくは油を用いる各種処理において、
操業中経時的に液体中にスラッジが蓄積し、液中に浮遊
混入する。このスラッジ除去は被処理材の処理効果を充
分高めるため、および処理後の品質を良好に維持するた
めに重大な関心が払われてきた事項である。すなわち、
スラッジの経時的増加により被処理材の処理品質が低下
するので、処理品質を回復することを目的として一定の
除滓サイクルが決定される。
In various treatments using molten salts, aqueous solutions or oils,
Sludge accumulates in the liquid over time during operation and becomes suspended in the liquid. This sludge removal has been a matter of great concern in order to sufficiently enhance the treatment effect of the treated material and to maintain good quality after treatment. That is,
Since the processing quality of the material to be processed deteriorates due to the increase in sludge over time, a certain sludge removal cycle is determined with the aim of restoring the processing quality.

従来、一般的に行われているスラッジの除去手段は金属
製の網または柄杓等で液体中のスラッジを補集除去する
か、フィルターによって濾過するか、あるいは処理槽の
底部に補集角皿(スラッジパン)を沈め、この上にスラ
ッジを沈降させて捕集するか、あるいはまた除去槽を処
理槽に取り付は補集したスラッジを定期的に取り出す等
により行われていた。
Conventionally, common methods for removing sludge include collecting and removing the sludge in the liquid using a metal net or ladle, filtering it with a filter, or installing a collection square dish ( This was done by sinking a sludge pan (sludge pan) onto which the sludge was allowed to settle and collecting it, or by attaching a removal tank to the treatment tank and periodically taking out the collected sludge.

〔発明が解決しようとする問題点〕[Problem that the invention seeks to solve]

しかしながら、上述のような従来技術において、人力に
よる補集では手間がかかる上に除去が不完全であり、フ
ィルターを用いる場合にはフィルターが詰り易く清掃ま
たは交換に手間がかかり、またスラッジパンによる場合
にはスラッジの沈降分離の間は本来の操業を中断しなけ
ればならず、さらに除去槽を処理槽に取り付は分離した
スラッジを定期的に取り出す装置にあっては補集スラッ
ジの取り出しに人手を要する上、処理槽の有効スペース
を減少する等の問題点を有する。さらに、これら従来技
術において、人力を要し、高温にさらされる溶融液の場
合は、危険な作業を操業者が行わなければならず、労働
安全上からも好ましくないものである。しがし、被処理
材の処理後の品質を良好に維持するためにこれらスラッ
ジ除去方法の実施を余儀なくされており、人力を要する
ことなく効率良くスラッジを分離除去し得る装置の出現
が待たれている現状にある。
However, in the conventional techniques described above, manual collection is time-consuming and removal is incomplete; when using a filter, the filter is easily clogged and cleaning or replacement is time-consuming; and when using a sludge pan, the removal is incomplete. In this case, the original operation must be interrupted during the sedimentation and separation of the sludge, and if the removal tank is attached to the treatment tank and the separated sludge is taken out periodically, it is necessary to manually take out the collected sludge. In addition, there are problems in that the effective space of the processing tank is reduced. Furthermore, these conventional techniques require manual labor, and in the case of a molten liquid exposed to high temperatures, the operator must perform dangerous work, which is undesirable from the standpoint of labor safety. However, in order to maintain good quality of treated materials after processing, it is necessary to implement these sludge removal methods, and the emergence of equipment that can efficiently separate and remove sludge without requiring human labor is awaited. The current situation is that

本発明はこれら従来の問題点を解消し、装置の操業を中
断することなく、従来の如何なる装置よりも効率の良い
スラッジ除去装置を提供することを目的とするものであ
る。
The present invention aims to solve these conventional problems and provide a sludge removal device that is more efficient than any conventional device without interrupting the operation of the device.

〔問題点を解決するための手段〕[Means for solving problems]

以上のような課題は、本発明によるスラッジ除去装置に
より達成される。
The above-mentioned problems are achieved by the sludge removal device according to the present invention.

すなわち、本発明は各種処理装置に併設され、これら処
理装置内のスラッジを含む液体をポンプ手段で汲上げ、
槽上方から槽内に供給する流入管およびスラッジ除去後
の液体を前記熱処理装置に還流する流出管を具え、槽内
にてスラッジを除去するスラッジ除去装置であって、前
記流入管がその漏斗状底部中心を外れた位置に開口する
逆円錐状底部を有する上室と、該上室底部中心から下方
に取り付けられた整流管と、スラッジの沈降が行われる
胴体部と、除去槽の底部を形成する逆円錐状のホッパー
と、ホッパーの下端頂部に取り付けられた弁および弁座
と、弁および弁座により開閉され外気に開口するスラッ
ジ排出管と、蓋とを具えたことを特徴とするものである
That is, the present invention is installed in various processing devices, pumps up liquid containing sludge in these processing devices with pump means,
A sludge removal device for removing sludge in the tank, comprising an inflow pipe that supplies the tank from above into the tank and an outflow pipe that returns the liquid after sludge removal to the heat treatment device, the inflow pipe having a funnel shape. An upper chamber having an inverted conical bottom that opens at a position off the center of the bottom, a rectifier pipe attached downward from the center of the bottom of the upper chamber, a body in which sludge settles, and a bottom of the removal tank. The hopper is characterized by comprising an inverted conical hopper, a valve and a valve seat attached to the top of the lower end of the hopper, a sludge discharge pipe that is opened and closed by the valve and valve seat and opens to the outside air, and a lid. be.

本発明の好ましい態様によれば、前記弁のステムが、弁
から垂直に上方に蓋より」二部にまで立ち上げられ、こ
のステムと弁の中心を貫通して設けた孔を通して詰り除
去棒が配設され、弁開閉用のハンドルがガイド管に穿孔
されたカム溝を貫通してステムに直角に固定され、ハン
ドルを水平方向に回転することにより前記カム溝に導か
れてハンドルとともにステムおよび弁が回転しつつ上昇
または下降し、弁を開閉するよう構成される。
According to a preferred embodiment of the invention, the stem of the valve is raised vertically upward from the valve to two parts above the lid, and a blockage removal rod is inserted through the stem and a hole provided through the center of the valve. A handle for opening and closing the valve passes through a cam groove bored in the guide tube and is fixed to the stem at right angles, and by rotating the handle horizontally, it is guided into the cam groove and opens the stem and valve together with the handle. The valve is configured to rotate and move up or down to open and close the valve.

本発明の他の態様によれば、前記装置が移動可能な台車
に載置される。
According to another aspect of the invention, the device is mounted on a movable trolley.

〔作  用〕[For production]

以上のような本発明のスラッジ除去装置は上記のように
構成され、この装置を用いて各種処理を行う処理槽中の
液体からスラッジを分離除去する場合を添付図面を参照
してその作用を説明する。
The sludge removal device of the present invention is constructed as described above, and its operation will be explained with reference to the attached drawings when this device is used to separate and remove sludge from liquid in a processing tank in which various treatments are performed. do.

まず、処理槽の底部に沈降したスラッジを含む液体はエ
アリフトポンプ等適宜の汲上げポンプ手段により連続的
に汲上げられ、その吐出管に接続された除去槽1の流入
管10を通って除去槽1の上室3の液面下に供給され、
この上室3で液体は鎮静化され、整流管4を降下し、下
部胴体部5に入る。液体は下部胴体部5の流路断面の拡
大により、その上昇速度は著しく減少し、流出管11よ
り処理槽に還流する。液体中に含まわているスラッジは
この過程において沈降して逆円錐状底部に沈殿濃縮され
、還流液中のスラッジは除去される。
First, the liquid containing the sludge that has settled at the bottom of the treatment tank is continuously pumped up by an appropriate pump means such as an air lift pump, and is passed through the inflow pipe 10 of the removal tank 1 connected to the discharge pipe of the liquid to the removal tank. 1 is supplied below the liquid level in the upper chamber 3,
The liquid is quenched in this upper chamber 3, descends through the rectifier tube 4, and enters the lower body portion 5. Due to the expansion of the cross section of the flow path in the lower body portion 5, the rising speed of the liquid is significantly reduced, and the liquid is returned to the processing tank through the outflow pipe 11. During this process, the sludge contained in the liquid settles and concentrates on the inverted conical bottom, and the sludge in the reflux liquid is removed.

本発明で対象とする液体とは、一般金属熱処理用の無機
混合塩等の溶融液、化成処理液、メツキ液等の水溶液も
しくは切削油、焼入油等の油をいい、例えば溶融液の場
合、使用中の比重は」。4〜2程度であり、このような
溶融液に金属製部品を浸漬加熱、浸炭、窒化する結果生
成する比重2.5〜6の微細なスラッジおよび汚泥が除
去しようとする対象物となる。すなわち、この比重差を
利用しスラッジ除去を行う過程において、溶融液が整流
管4および胴体部5の沈降部を通過する際の流速および
通過時間は重要な因子であって、整流管4においては通
過速度が1.m/mjn以下で、通過時間が10秒以上
の場合は整流効果が良く、通過速度が1 m / m、
inを超える場合は濃縮部に濃縮されたスラッジを巻き
上げる現象を生じ、通過時間が10秒より短いと沈降部
のスラッジの沈降を乱し、沈降力離の効果を低下させる
The liquid targeted by the present invention refers to a molten liquid such as an inorganic mixed salt for general metal heat treatment, an aqueous solution such as a chemical conversion liquid, a plating liquid, or an oil such as cutting oil or quenching oil. For example, in the case of a molten liquid , the specific gravity in use is”. The objects to be removed are fine sludge and sludge with a specific gravity of 2.5 to 6, which are produced as a result of immersing metal parts in such a molten liquid and heating, carburizing, and nitriding. That is, in the process of removing sludge using this specific gravity difference, the flow velocity and passage time of the melt when it passes through the rectifier tube 4 and the settling section of the body section 5 are important factors. The passing speed is 1. m/mjn or less and the passing time is 10 seconds or more, the rectification effect is good, and the passing speed is 1 m/m,
If it exceeds in, a phenomenon occurs in which the concentrated sludge is rolled up in the concentrating section, and if the passing time is shorter than 10 seconds, the settling of the sludge in the settling section is disturbed, reducing the effect of settling force separation.

整流管4の寸法構造が上記条件を満たしている場合でも
、溶融液の沈降部における上昇速度が0.06m/mi
n以下で、通過時間が5分以上の二つの条件を同時に満
足させることがスラッジの良好な沈降をもたらすために
好ましい。
Even if the dimensional structure of the rectifier tube 4 satisfies the above conditions, the rising speed of the melt at the settling part is 0.06 m/mi.
It is preferable to simultaneously satisfy the two conditions of n or less and passage time of 5 minutes or more in order to achieve good sedimentation of the sludge.

ハンドルガイド管]4にくり抜かれた傾斜したカム溝1
5を通って弁7のステム12に直角に固定されたハンド
ル9を水平方向に操作すると、カム溝15の傾斜に沿っ
てハンドル9が上昇または下降するので、ハンドル9と
一体になっているステム12および弁7も回転しつつ上
昇または下降し、それにより弁7は容易にかつ確実に開
閉する。この弁操作によりスラッジは排出管J3を通っ
て排出管開口部の下方に用意したスラッジ受は皿]7に
抜き取られる。
Handle guide tube] Slanted cam groove 1 hollowed out in 4
When the handle 9 fixed perpendicularly to the stem 12 of the valve 7 through the cam groove 5 is operated in the horizontal direction, the handle 9 moves up or down along the slope of the cam groove 15. 12 and the valve 7 also move up or down while rotating, whereby the valve 7 opens and closes easily and reliably. By operating this valve, the sludge passes through the discharge pipe J3 and is drawn out into the sludge tray 7 provided below the discharge pipe opening.

スラッジ排出管内に固形ソルトが析出しスラッジの排出
が円滑に行わ才しないときは、槽底の弁およびそのステ
ムの中心に穿孔された孔を利用して貫通挿入されノ已ス
ラッジ詰り除去棒16を上下させ、固形ツルl−を除去
することができる。
If solid salt is precipitated in the sludge discharge pipe and the sludge cannot be discharged smoothly, the sludge clog removal rod 16 is inserted through the valve at the bottom of the tank and the hole drilled in the center of its stem. It can be moved up and down to remove solid vines l-.

溶融液の場合はスラッジ除去槽の液温ば、配設された加
熱および温度?A節手段を有する炉2によって熱処理溶
融液槽の温度と同等以」二の一定温度に保持される。ま
た、流入管10の大気接触部は断熱材により被覆保温さ
れ、流出管11の大気接触部は加熱および温度調節手段
を有する被覆により流出溶融液の温度を一定に調節し、
冷却によりツルI・が析出して管路を閉塞することを防
止する。さらに、スラッジ除去槽には、流出管の万一の
閉塞により流入液の描出を防止するための液面の異常」
二昇を検知警報するためのセンサーとして熱電対19ま
たは液面計が設けられろ。
In the case of molten liquid, what is the temperature of the liquid in the sludge removal tank, the installed heating and temperature? The furnace 2 having section A means is maintained at a constant temperature equal to or greater than the temperature of the heat treatment melt bath. In addition, the air contact portion of the inflow pipe 10 is coated and kept warm with a heat insulating material, and the air contact portion of the outflow pipe 11 is coated with heating and temperature control means to keep the temperature of the flowing melt constant.
Cooling prevents vines I from precipitating and clogging the pipes. In addition, there is an abnormality in the liquid level in the sludge removal tank to prevent the inflow liquid from being drawn in the event of a blockage of the outflow pipe.
A thermocouple 19 or a liquid level gauge should be provided as a sensor to detect and alarm the second rise.

なお、本装置はキャスター等により移動可能とした台車
18上に載置すれば複数の処理槽のスラッジ除去を1台
のスラッジ除去装置で兼ねることができる。
Note that if this device is placed on a cart 18 that is movable with casters or the like, one sludge removing device can remove sludge from a plurality of treatment tanks.

以上説明したスラッジ除去装置は本来の処理槽の操業を
まったく妨げることなく操作することができる]二、ス
ラッジの排出操作以外はまったく自動運転であり、人力
を要する部分も自動化機構を付加しプログラム化するこ
とにより、容易に全自動化することも可能である。
The sludge removal equipment described above can be operated without interfering with the original operation of the treatment tank]2.Everything other than the sludge discharge operation is completely automatic, and parts that require human power are also programmed with automation mechanisms added. By doing so, it is possible to easily fully automate the process.

〔実施例〕〔Example〕

塩浴軟窒化槽のスラッジ除去に本発明装置を使用した場
合と、従来行われているスラッジパン方式を使用した場
合との結果を比較すると第1表のようになる。
Table 1 shows a comparison of the results when the apparatus of the present invention is used to remove sludge from a salt bath nitrocarburizing tank and when the conventional sludge pan method is used.

本発明装置を使用した場合における塩浴軟窒化槽よりス
ラッジ除去槽へのスラッジを含む溶融液の汲上げ手段は
ニアリフI〜ポンプを使用した。
When the apparatus of the present invention was used, a Nearlift I pump was used as a means for pumping up the molten liquid containing sludge from the salt bath nitrocarburizing tank to the sludge removal tank.

(以下余白) 本発明装置において、表に示す実施例の寸法の場合は、
汲上げソルトの除去槽への流入速度は72〜180 Q
 / Hの範囲内で実施し、スラッジの沈降分離は良好
であった。
(Margins below) In the device of the present invention, in the case of the dimensions of the embodiment shown in the table,
The flow rate of pumped salt into the removal tank is 72 to 180 Q.
/H, and the sedimentation and separation of the sludge was good.

この時の整流管を通過する溶融液の流速は0.35〜0
.88m /min、通過時間は29〜12secで、
沈降部を上昇する溶融液の速度は0.019〜0.04
9m/min、通過時間は15.7〜6.2m1nであ
った。
The flow rate of the melt passing through the rectifier tube at this time is 0.35 to 0.
.. 88m/min, passing time is 29~12sec,
The velocity of the melt rising through the settling section is 0.019 to 0.04
The speed was 9 m/min, and the passing time was 15.7 to 6.2 m1n.

第1表の成績を比較すると、表に示す実施態様の下で、
本発明による除滓効果はスラッジパン方式に比較して、
約22%向」ニした上、熱処理槽の稼働時間に対し、従
来法は2時間の停止を余儀なくされるが、本発明装置で
は停止時間はOであり、生産効率を著しく向上させてい
る。
Comparing the results in Table 1, under the implementation shown in the table,
Compared to the sludge pan method, the sludge removal effect of the present invention is
In addition, the conventional method requires a two-hour stoppage compared to the operating time of the heat treatment tank, but the apparatus of the present invention requires a stoppage time of 0, significantly improving production efficiency.

〔効  果〕〔effect〕

以上のような本発明によれば、処理槽の稼働をまったく
妨げることなく、その液封中のスラッジを従来の如何な
る装置よりも効率良く分離除去することができる。また
、本装置を稼働するのに要する労力は従来の如何なる装
置に比較しても少なくてよい。
According to the present invention as described above, the sludge in the liquid seal can be separated and removed more efficiently than any conventional device without interfering with the operation of the treatment tank at all. Additionally, the effort required to operate the device is less than any conventional device.

さらに5本装置により、労働安全上の問題が改善され、
安定した品質が得られる。また、スラッジ排出弁の操作
等に自動化機構を付加すれば、容易に無人化することも
可能なものである。
In addition, the five devices have improved occupational safety issues,
Stable quality can be obtained. Furthermore, by adding an automation mechanism to the operation of the sludge discharge valve, etc., it is possible to easily make the system unmanned.

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

第1図は、本発明に係る溶融液中のスラッジ除去装置を
一部透視図で示した概略縦断面図である。 1・・・スラッジ除去槽 3・・・上室 5・・・胴体部 7・・・弁 9・・・ハンドル 11・・・流出管 13・・・排出管 15・カム溝 17・・・スラッジ受は皿 19・・熱電対 2・・・保温炉 4・・・整流管 6・・・ホッパー 8・・・弁座 10・・・流入管 12・・・ステム 14・・・ガイド管 16・・・詰り除去棒 18・・・台車 20・・・炉蓋
FIG. 1 is a schematic vertical cross-sectional view showing a partially transparent view of an apparatus for removing sludge in a melt according to the present invention. 1...Sludge removal tank 3...Upper chamber 5...Body part 7...Valve 9...Handle 11...Outflow pipe 13...Discharge pipe 15/Cam groove 17...Sludge The receiver is a plate 19...thermocouple 2...warming furnace 4...straightening tube 6...hopper 8...valve seat 10...inflow pipe 12...stem 14...guide pipe 16.・Clog removal rod 18 ・Dolly 20 ・Hearth lid

Claims (1)

【特許請求の範囲】 1、各種処理装置に併設され、該処理装置内のスラッジ
を含む液体をポンプ手段で汲上げ、槽上方から槽内に供
給する流入管およびスラッジ除去後の液体を前記処理装
置に還流する流出管を具え、槽内にてスラッジを除去す
るスラッジ除去装置であって、前記流入管がその漏斗状
底部中心を外れた位置に開口する逆円錐状底部を有する
上室と、該上室底部中心から下方に取り付けられた整流
管と、スラッジの沈降が行われる胴体部と、除去槽の底
部を形成する逆円錐状のホッパーと、ホッパーの下端頂
部に取り付けられた弁および弁座と、弁および弁座によ
り開閉され外気に開口するスラッジ排出管と、蓋とを具
えたことを特徴とするスラッジ除去装置。 2、前記弁のステムが、弁から垂直に上方に蓋より上部
にまで立ち上げられ、このステムと弁の中心を貫通して
設けた孔を通して詰り除去棒が配設され、弁開閉用のハ
ンドルがガイド管に穿孔されたカム溝を貫通してステム
に直角に固定され、ハンドルを水平方向に回転すること
により前記カム溝に導かれてハンドルとともにステムお
よび弁が回転しつつ上昇または下降し、弁を開閉するよ
う構成されている請求項1記載のスラッジ除去装置。 3、装置が移動可能な台車に載置された請求項1または
2記載のスラッジ除去装置。
[Scope of Claims] 1. An inflow pipe that is attached to various processing equipment, pumps up the liquid containing sludge in the processing equipment and supplies it into the tank from above the tank, and the liquid after the sludge is removed is used for the above-mentioned processing. A sludge removal device for removing sludge in a tank, comprising an outflow pipe that returns to the device, the upper chamber having an inverted conical bottom with the inflow pipe opening at a position off the center of the funnel-shaped bottom; A rectifier pipe attached downward from the center of the bottom of the upper chamber, a body section where sludge settles, an inverted conical hopper forming the bottom of the removal tank, and a valve attached to the top of the lower end of the hopper. A sludge removal device comprising a seat, a valve and a sludge discharge pipe opened and closed to the outside air by the valve seat, and a lid. 2. The stem of the valve is raised vertically upward from the valve to the top of the lid, and a blockage removal rod is disposed through a hole made through the stem and the center of the valve, and a handle for opening and closing the valve is provided. passes through a cam groove bored in the guide tube and is fixed to the stem at right angles, and when the handle is rotated horizontally, it is guided to the cam groove and the stem and valve are rotated together with the handle and raised or lowered, The sludge removal device according to claim 1, wherein the sludge removal device is configured to open and close a valve. 3. The sludge removal device according to claim 1 or 2, wherein the device is mounted on a movable trolley.
JP2154009A 1990-06-14 1990-06-14 Sludge removal device Expired - Lifetime JPH0647043B2 (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
JP2154009A JPH0647043B2 (en) 1990-06-14 1990-06-14 Sludge removal device

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
JP2154009A JPH0647043B2 (en) 1990-06-14 1990-06-14 Sludge removal device

Publications (2)

Publication Number Publication Date
JPH0445803A true JPH0445803A (en) 1992-02-14
JPH0647043B2 JPH0647043B2 (en) 1994-06-22

Family

ID=15574917

Family Applications (1)

Application Number Title Priority Date Filing Date
JP2154009A Expired - Lifetime JPH0647043B2 (en) 1990-06-14 1990-06-14 Sludge removal device

Country Status (1)

Country Link
JP (1) JPH0647043B2 (en)

Citations (5)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JPS495062U (en) * 1972-04-13 1974-01-17
JPS513650U (en) * 1974-06-26 1976-01-12
JPS5135848U (en) * 1974-09-09 1976-03-17
JPS51161683U (en) * 1975-06-17 1976-12-23
JPS6183403U (en) * 1984-11-02 1986-06-02

Patent Citations (5)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JPS495062U (en) * 1972-04-13 1974-01-17
JPS513650U (en) * 1974-06-26 1976-01-12
JPS5135848U (en) * 1974-09-09 1976-03-17
JPS51161683U (en) * 1975-06-17 1976-12-23
JPS6183403U (en) * 1984-11-02 1986-06-02

Also Published As

Publication number Publication date
JPH0647043B2 (en) 1994-06-22

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