JPS6012082B2 - Portable solid-liquid separator - Google Patents

Portable solid-liquid separator

Info

Publication number
JPS6012082B2
JPS6012082B2 JP52075420A JP7542077A JPS6012082B2 JP S6012082 B2 JPS6012082 B2 JP S6012082B2 JP 52075420 A JP52075420 A JP 52075420A JP 7542077 A JP7542077 A JP 7542077A JP S6012082 B2 JPS6012082 B2 JP S6012082B2
Authority
JP
Japan
Prior art keywords
tank
water
flocculant
flocculation reaction
reaction tank
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
Application number
JP52075420A
Other languages
Japanese (ja)
Other versions
JPS5410473A (en
Inventor
保 小川
滋豊 坂井
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.)
Hitachi Construction Machinery Co Ltd
Original Assignee
Hitachi Construction Machinery 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 Hitachi Construction Machinery Co Ltd filed Critical Hitachi Construction Machinery Co Ltd
Priority to JP52075420A priority Critical patent/JPS6012082B2/en
Publication of JPS5410473A publication Critical patent/JPS5410473A/en
Publication of JPS6012082B2 publication Critical patent/JPS6012082B2/en
Expired legal-status Critical Current

Links

Description

【発明の詳細な説明】 本発明は、運搬、据付および保守点検容易な可搬式団液
分離装置に関するものである。
DETAILED DESCRIPTION OF THE INVENTION The present invention relates to a portable liquid mass separation device that is easy to transport, install, and maintain.

従来のこの種の固液分離装置は、シックナ、脱水機、凝
集剤溶解槽、凝集剤貯槽および一次、二次凝集反応槽な
どを個々に設置すると共に、その間を配管で接続して現
場に裾付けていた。
Conventional solid-liquid separation equipment of this type has a thickener, dehydrator, flocculant dissolution tank, flocculant storage tank, primary and secondary flocculation reaction tanks, etc. installed individually, and is connected to the site with piping. I was wearing it.

このため大きな設置面積を要し、かつ現場における設遺
作業に多くの時間と多額の費用とがかかる欠点がある。
この欠点を改善するため、本出願人は、特磯昭50−5
5123号(椿閥昭52−5994y号)の泥水処理装
置を提案した。
For this reason, it requires a large installation area, and has the disadvantage that construction work on site requires a lot of time and a large amount of cost.
In order to improve this drawback, the applicant has proposed
We proposed muddy water treatment equipment No. 5123 (Tsubakitsu No. 52-5994y).

この装置によれば、分割できる上下二つの枠体に泥水処
理装置として必要な機器を一つのブロックに分けて取付
け、運搬輸送可能で、しかも大きな設置面積を要しない
泥水処理装置を提供できる。また、両枠体上の機器間を
現地にて接続すれば良いので、設置作業を短時間に行え
る利点がある。しかし、二つのブロックを別々に運搬輸
送すると共に、それらの機器間の接続等の設置作業を現
地にて行わなければならず、移設の頻繁な士木蓮設工事
に充分対応できない難点がある。また、泥水処理装贋の
作動中は、シックナ内に常時給水する必要があり、その
設備および保守点検が面倒であった。前記二つのブロッ
クの各機器間の接続作業などを現地で行なわないですむ
ようにするため、すべての機器を同一フレーム上に配設
することが考えられる。
According to this device, the necessary equipment for the muddy water treatment device is attached in one block to the two upper and lower frames that can be divided, and it is possible to provide a muddy water treatment device that is transportable and does not require a large installation area. Furthermore, since it is only necessary to connect the devices on both frames on-site, there is an advantage that the installation work can be completed in a short time. However, the two blocks must be transported separately, and installation work such as connections between the devices must be carried out on site, which has the disadvantage that it cannot adequately handle the construction work of magnolias, which requires frequent relocation. Furthermore, while the muddy water treatment equipment is in operation, it is necessary to constantly supply water into the thickener, making the equipment and maintenance inspection troublesome. In order to eliminate the need to perform on-site connection work between the devices of the two blocks, it is conceivable to arrange all the devices on the same frame.

しかし、輸送車鋼の搭載可能な面積には限度があって、
前記二つのブロックのすべての機器を同一フレーム上に
配談すると輸送可能な面積内におさめることは不可能で
ある。さらに、脱水機から排出される炉液の処理にも問
題がある。本発明は、上記先顕発明を改良し、輸送可能
な面積のフレーム上にすべての機器を合理的に配設して
、設置作業を必要としないコンパクトな可搬式固液分離
装置を提供すると共に、処理水を循環させて作業中の給
水を不要ならしめたものである。本発明は、上記の目的
を達成するため、シックナの上部にこれと一体的に三角
せきを備えた泥水導入槽および一次凝集反応槽を設けて
泥水導入槽および一次凝集反応槽のフレームへの取付け
面積を不要とし、また「第二凝集剤貯槽の上部に第二凝
集剤溶解槽を設けて第二凝集剤熔解槽のフレームへの取
付け面積を不要とし、さらに、脱水機の下部に炉液受槽
を配設すると共にその炉液受槽中の炉液をポンプおよび
配管を介して一次凝集反応槽に戻し、かつ、その一次凝
集反応槽に連続するシックナの上燈水を第一、第二凝集
剤溶解槽の溶解水および前記脱水機の炉布洗浄水として
循環使用し、作業中における給水を不必要ならしめたこ
とを特徴とする。
However, there is a limit to the area that can be loaded with transport vehicle steel.
If all the equipment of the two blocks were arranged on the same frame, it would be impossible to fit them within a transportable area. Furthermore, there are also problems in the treatment of furnace liquid discharged from the dehydrator. The present invention improves the above-mentioned prior invention, and provides a compact, portable solid-liquid separation device that does not require installation work by rationally arranging all equipment on a frame with a transportable area. , which circulates treated water and eliminates the need for water supply during work. In order to achieve the above object, the present invention provides a muddy water introduction tank and a primary flocculation reaction tank integrally equipped with a triangular weir in the upper part of the thickener, and attaches the muddy water introduction tank and the primary flocculation reaction tank to the frame. In addition, a second flocculant dissolving tank is provided above the second flocculant storage tank to eliminate the need for installation area on the frame of the second flocculant dissolving tank, and a furnace liquid receiving tank is installed at the bottom of the dehydrator. At the same time, the furnace liquid in the furnace liquid receiving tank is returned to the primary flocculation reaction tank via a pump and piping, and the thickener top water connected to the primary flocculation reaction tank is used as a first and second flocculant. It is characterized in that it is circulated and used as dissolving water in the dissolving tank and washing water for the furnace cloth in the dehydrator, thereby eliminating the need for water supply during work.

以下、本発明の可磯式固液分離装置の一実施例を第1図
ないし第6図により説明する。
DESCRIPTION OF THE PREFERRED EMBODIMENTS An embodiment of the solid-liquid separator according to the present invention will be described below with reference to FIGS. 1 to 6.

本発明の園液分離装置は、シックナ5と、第一凝集剤(
例えば、無機系凝集剤)を貯え溶解する貯槽兼第一凝集
剤容鰯槽9と、第二凝集剤(例えば、高分子凝集剤)を
貯える貯槽11と、二次凝集反応槽6と、脱水機7と、
前記各機器の操作を行う電気制御盤17とを同一フレー
ム上に設置する。
The garden liquid separation device of the present invention includes a thickener 5 and a first flocculant (
For example, a storage tank/first flocculant tank 9 that stores and dissolves an inorganic flocculant (inorganic flocculant), a storage tank 11 that stores a second flocculant (for example, a polymer flocculant), a secondary flocculation reaction tank 6, and a dehydration tank. Machine 7 and
An electric control panel 17 for operating each of the devices is installed on the same frame.

前記シックナ5は、上部に三角せきを備えた泥水導入槽
3および溢流せき5aを設けると共に、上方内部の一部
を区切って一次凝集反応糟4を設け、底部に雛泥ます5
bを設けると共に回転集泥具18を装備し、これにより
泥水導入槽3および一次凝集反応槽4のフレームへの取
付け面積を不要とする。
The thickener 5 is provided with a mud water introduction tank 3 and an overflow weir 5a equipped with a triangular weir at the top, a primary flocculation reaction chamber 4 is provided by dividing a part of the upper interior, and a chick mud basin 5 at the bottom.
b and is also equipped with a rotating mud collecting device 18, thereby eliminating the need for mounting areas for the muddy water introduction tank 3 and the primary flocculation reaction tank 4 on the frame.

なお、前記シックナ5は、第1図および第2図に示すよ
うに、輸送限界中で表面積を最も広くとれる角型のもの
とする。また、貯槽11の上部には第二凝集剤溶解槽1
0を設け、これにより第二凝集剤溶解槽10のフレーム
への取付け面積を不要とする。
As shown in FIGS. 1 and 2, the thickener 5 has a rectangular shape that has the largest surface area within the transport limit. In addition, a second flocculant dissolving tank 1 is provided in the upper part of the storage tank 11.
0 is provided, thereby eliminating the need for an area for attaching the second coagulant dissolving tank 10 to the frame.

脱水機7は、下部に炉布洗浄水および脱水炉液を受ける
炉液受槽8を設ける。
The dehydrator 7 is provided with a furnace liquid receiving tank 8 at its lower portion for receiving furnace cloth washing water and dehydrating furnace liquid.

前記第一凝集剤溶解槽9と前記三角せきを備えた泥水導
入槽3との闇を注入ポンプ12を介して配管し、前記貯
槽11と前記一次凝集反応槽4および二次凝集反応槽6
との間を注入ポンプ13および14を介して配管し、前
記二次凝集反応槽6と前記シックナ5との間を給泥ポン
プ15を介して配管し、前記炉液受槽8内に設置した炉
液ポンプ16より前記一次凝集反応槽4に配管し、前記
シックナ5の上燈水を脱水機7の炉布洗浄水および凝集
剤溶解水として用いるためL ポンプ21,マニホルド
22を介してジェットノズル19、貯槽兼第一凝集剤客
解槽9および第二凝集剤溶解槽10へ配管する。
The first flocculant dissolving tank 9 and the muddy water introduction tank 3 equipped with the triangular weir are connected through an injection pump 12, and the storage tank 11, the primary flocculation reaction tank 4, and the secondary flocculation reaction tank 6 are connected to each other via an injection pump 12.
A furnace installed in the furnace liquid receiving tank 8, with piping connected between the secondary flocculation reaction tank 6 and the thickener 5 through a mud supply pump 15, and a furnace installed in the furnace liquid receiving tank 8. A liquid pump 16 is connected to the primary flocculation reaction tank 4, and the top water from the thickener 5 is used as furnace cloth cleaning water and flocculant dissolving water for the dehydrator 7. , piping is connected to a storage tank/first flocculant dissolution tank 9 and a second flocculant dissolution tank 10.

さらに前記ポンプ21を利用し、作動開始時に必要な水
を外部水源23よりシックナ5内に取入れると共に、作
動完了後シックナ5内の残水を外部へ放出し得るように
配管する。
Further, by using the pump 21, necessary water is taken into the thickener 5 from an external water source 23 at the start of operation, and piping is provided so that the remaining water in the thickener 5 can be discharged to the outside after the operation is completed.

図中、20‘ま泥水槽で、内部に給水ポンプーを設置し
、その給水ポンプ1に接続した給水管を流量調整弁2を
介して前記三角せきを備えた泥水導入槽3に接続する。
In the figure, 20' is a mud water tank, a water supply pump is installed inside, and a water supply pipe connected to the water supply pump 1 is connected via a flow rate regulating valve 2 to the mud water introduction tank 3 equipped with the triangular weir.

本発明の固液分離装置は、上記の如き構成よりなり、以
下述べるようにして固液分離する。まず、第4図に示す
ように、シックナ5内に外部水源23より水を取入れ、
次に給水ポンプーを作動させて泥水槽20内の泥水を三
角せきを備えた泥水導入槽3に送る。すると、泥水導入
槽3に第一凝集剤が注入ポンプ12により貯槽兼第一凝
集剤客解槽9から注入され、さらに一次凝集反応槽4内
に第二凝集剤が注入ポンプ13により貯槽11から注入
され、泥水と凝集剤とが混合櫨拝されて凝集反応しなが
らシックナ5内に流れ込む。凝集反応により生成したフ
ロックはシックナ5の底部に沈降して回転集泥具18に
より排泥ます5bに集められ、給泥ポンプ15により二
次凝集反応槽6内に送られ、この二次凝集反応槽6にお
いて注入ポンプ14により貯槽11から第二凝集剤が注
入され、さらに二次凝集反応槽6で混合燈拝されて脱水
に通したフロツクに生成される。前記第二次凝集反応槽
6より脱水機7に送られたフロックはベルトによりプレ
スされ、脱水ケーキと炉液とに分離され、脱水ケーキは
シュートを経て装置外に排出され、一方炉液は、炉布洗
浄水と共に炉液受槽8内に送られる。そして、前記炉液
受槽8内の炉液および炉布洗浄水は炉液ポンプ16によ
り一次凝集反応糟4内に戻される。
The solid-liquid separator of the present invention has the configuration described above, and performs solid-liquid separation as described below. First, as shown in FIG. 4, water is introduced into the thickener 5 from the external water source 23.
Next, the water supply pump is operated to send the muddy water in the muddy water tank 20 to the muddy water introducing tank 3 equipped with a triangular weir. Then, the first flocculant is injected into the muddy water introduction tank 3 from the storage tank/first flocculant disassembly tank 9 by the injection pump 12, and the second flocculant is injected into the primary flocculation reaction tank 4 from the storage tank 11 by the injection pump 13. The muddy water and flocculant are mixed and flow into the thickener 5 while undergoing a coagulation reaction. The flocs generated by the flocculation reaction settle to the bottom of the thickener 5, are collected in the mud draining basin 5b by the rotating mud collecting device 18, and are sent into the secondary flocculation reaction tank 6 by the mud supply pump 15, where the flocs are fed to the secondary flocculation reaction tank 6. In the tank 6, the second flocculant is injected from the storage tank 11 by the injection pump 14, and further mixed in the secondary flocculation reaction tank 6 to form a floc which has been subjected to dewatering. The flocs sent from the second coagulation reaction tank 6 to the dehydrator 7 are pressed by a belt and separated into a dehydrated cake and a furnace liquid.The dehydrated cake is discharged outside the apparatus through a chute, while the furnace liquid is It is sent into the furnace liquid receiving tank 8 together with the furnace cloth cleaning water. The furnace liquid and furnace cloth cleaning water in the furnace liquid receiving tank 8 are returned to the primary flocculation reaction chamber 4 by the furnace liquid pump 16.

一方、前記シックナ5内においてフロックと分離された
上燈水は、第5図に示すように、ポンプ21により吸上
げられてマニホルド22により分岐され、バルブ24の
開閉により貯槽兼第一凝集剤客鱗槽9および第二凝集剤
溶解槽101こ溶解水として供孫台されると共に、脱水
機7のジェットノズル19に炉布洗浄水として供給され
る。作業が終了したならば、第6図に示すように、シツ
クナ5内に残った水をポンプ21により吸上げてマニホ
ルド22を経て外部に放出する。
On the other hand, the water separated from the flocs in the thickener 5 is sucked up by a pump 21 and branched by a manifold 22, as shown in FIG. The scale tank 9 and the second flocculant dissolving tank 101 are supplied as dissolving water, and are also supplied to the jet nozzle 19 of the dehydrator 7 as furnace cloth washing water. When the work is completed, as shown in FIG. 6, the water remaining in the water bottle 5 is sucked up by the pump 21 and discharged to the outside through the manifold 22.

ポンプ21は、上記のように、外部水源23からシツク
ナ5へ給水と、シックナ5からジェット/ズル19、貯
槽兼第一凝集剤客解槽9および第二凝集剤溶解槽10へ
の給水と、作業完了後のシックナ5内の残水を外部へ放
出することを行う。このように、本発明においては、シ
ツクナの上部にこれと一体的に三角せきを備えた泥水導
入槽および一次凝集反応槽を設けて泥水導入槽および一
次凝集反応糟のフレームへの取付け面積を不要とし、ま
た、第二凝集剤貯槽の上部に第二凝集剤溶解槽を設けて
第二凝集剤溶解槽のフレームへの取付け面積を不要とし
たので、固液分離装置として必要とするすべての機器を
輪送可能な面積内の1つのフレームに配議することがで
き、これにより、移設の頻繁な土木建設工事現場におけ
る配管作業を省略して直ちに作業を行なうことができる
As described above, the pump 21 supplies water from the external water source 23 to the thickener 5, and from the thickener 5 to the jet/thrower 19, the storage tank/first flocculant dissolving tank 9, and the second flocculant dissolving tank 10. After the work is completed, the remaining water in the thickener 5 is discharged to the outside. In this way, in the present invention, the muddy water introduction tank and the primary flocculation reaction tank are provided integrally with the triangular weir in the upper part of the Shitsukuna, thereby eliminating the need for mounting area for the muddy water introduction tank and the primary flocculation reaction tank on the frame. In addition, the second flocculant dissolving tank is installed above the second flocculant storage tank, eliminating the need for the installation area of the second flocculant dissolving tank to the frame, so all the equipment required as a solid-liquid separator can be removed. can be arranged in one frame within the area that can be wheeled, thereby allowing work to be carried out immediately without piping work at civil engineering construction sites where relocation is frequent.

また本発明は、脱水機の下部に特に炉液受槽を配設し、
その受槽中の炉液をポンプおよび配管を介してシックナ
の上部の一次凝集反応槽に戻し、かつそのシックナの上
澄水を第一,第二凝集剤溶解槽の溶解水および脱水機の
炉布洗浄水として循環使用するようにしたので、作業中
における外部からの給水を不要にすることができる。
Further, the present invention particularly provides a furnace liquid receiving tank in the lower part of the dehydrator,
The furnace liquid in the receiving tank is returned to the primary flocculation reaction tank at the top of the thickener via the pump and piping, and the supernatant water from the thickener is used to wash the dissolved water of the first and second flocculant dissolution tanks and the furnace fabric of the dehydrator. Since the water is recycled, there is no need to supply water from outside during work.

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

添付図面は本発明に係る固液分離装置の一実施例を示し
、第1図は平面図、第2図は側面図、第3図は処理シス
テム図、第4図,第5図および第6図は作動開始時,作
動時および作動完了時の各々の場合の水の流れを示した
説明図である。 3・・・・・・三角せきを備えた泥水導入槽、4・・・
・・・一次凝集反応槽、5…・・・シツクナ、6・・・
二次凝集反応槽、7・・・・・・脱水機、8・・・…炉
液受槽、9……貯槽兼第一凝集剤客解槽、10……第二
凝集剤溶解槽、11……貯槽、1,12,13,14,
15,16,21……ポンプ、17……電気制御盤、1
9……ジェットノズル、22……マニホルド。 第1図 第2図 第3図 第4図 第5図 第6図
The attached drawings show an embodiment of the solid-liquid separation device according to the present invention, in which Fig. 1 is a plan view, Fig. 2 is a side view, Fig. 3 is a treatment system diagram, and Figs. 4, 5, and 6. The figure is an explanatory diagram showing the flow of water at the start of operation, at the time of operation, and at the end of operation. 3... Mud water introduction tank equipped with a triangular weir, 4...
...Primary flocculation reaction tank, 5...Shitsukuna, 6...
Secondary flocculation reaction tank, 7... Dehydrator, 8... Furnace liquid receiving tank, 9... Storage tank/first flocculant dissolution tank, 10... Second flocculant dissolution tank, 11... ...Storage tank, 1, 12, 13, 14,
15, 16, 21...pump, 17...electric control panel, 1
9... Jet nozzle, 22... Manifold. Figure 1 Figure 2 Figure 3 Figure 4 Figure 5 Figure 6

Claims (1)

【特許請求の範囲】[Claims] 1 三角せきを備えた泥水導入槽および一次凝集反応槽
を上部に備えたシツクナと、前記泥水導入槽に注入する
第一凝集剤の貯槽兼容解槽と、前記シツクナの底部に沈
降したフロツクを導入する二次凝集反応槽と、前記一次
凝集反応槽および前記二次凝集反応槽にそれぞれ注入す
る第二凝集剤を貯えると共にその第二凝集剤を溶解する
第二凝集剤溶解槽を上部に備えた貯槽と、下部に濾布洗
浄水および脱水濾液を受ける濾液受槽を備えると共に前
記二次凝集反応槽内で撹拌されたフロツクを送り込んで
脱水を行わせる脱水機と、各機器に操作を行う電気制御
盤とを同一フレーム上に設置し、前記濾液受槽内の濾液
および先浄水を前記一次凝集反応槽に戻すポンプおよび
配管を施し、前記シツクナの上澄水を前記第一、第二凝
集剤溶解槽の溶解水および前記脱水機の濾布洗浄水とし
て供給するポンプおよび配管を施し、作動開始時に必要
な水を外部から前記シツクナ内に取入れると共に、作動
完了後前記シツクナ内の水を外部に放出できるように構
成したことを特徴とする可搬式固液分離装置。
1. Introduce a mud water introduction tank equipped with a triangular weir and a primary flocculation reaction tank at the top, a storage tank and dissolution tank for the first flocculant to be injected into the mud water introduction tank, and the settled flocs at the bottom of the rock tank. a second flocculant dissolving tank that stores a second flocculant to be injected into the first flocculation reaction tank and the second flocculant, respectively, and dissolves the second flocculant. A dehydrator which includes a storage tank, a filtrate receiving tank at the bottom for receiving filter cloth washing water and dehydrated filtrate, and which sends floc stirred in the secondary flocculation reaction tank to perform dehydration, and electric control to operate each device. A pump and piping are installed to return the filtrate and pre-purified water in the filtrate receiving tank to the primary flocculation reaction tank, and the supernatant water of the Shitukuna is transferred to the first and second flocculant dissolution tanks. A pump and piping are installed to supply water dissolved in water and filter cloth washing water for the dehydrator, and necessary water is taken into the strainer from the outside at the start of operation, and water in the strainer is discharged to the outside after the operation is completed. A portable solid-liquid separator characterized in that it is configured to be able to
JP52075420A 1977-06-23 1977-06-23 Portable solid-liquid separator Expired JPS6012082B2 (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
JP52075420A JPS6012082B2 (en) 1977-06-23 1977-06-23 Portable solid-liquid separator

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
JP52075420A JPS6012082B2 (en) 1977-06-23 1977-06-23 Portable solid-liquid separator

Publications (2)

Publication Number Publication Date
JPS5410473A JPS5410473A (en) 1979-01-26
JPS6012082B2 true JPS6012082B2 (en) 1985-03-29

Family

ID=13575670

Family Applications (1)

Application Number Title Priority Date Filing Date
JP52075420A Expired JPS6012082B2 (en) 1977-06-23 1977-06-23 Portable solid-liquid separator

Country Status (1)

Country Link
JP (1) JPS6012082B2 (en)

Families Citing this family (6)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JPS60162939A (en) * 1984-02-03 1985-08-24 Ulvac Corp Automatic alignment adjusting device of optical measurement system
JPS60263817A (en) * 1984-06-12 1985-12-27 Victor Co Of Japan Ltd Elliptic polarizer using rotary analyzer
JPS612028A (en) * 1984-06-15 1986-01-08 Victor Co Of Japan Ltd Method for detecting phase difference between rotary analyser and rotary phase detecting element in elliptic polarizer
JPS62267625A (en) * 1986-05-15 1987-11-20 Japan Spectroscopic Co Ellipsometer
JPS63107837U (en) * 1986-12-30 1988-07-12
JP2564759B2 (en) * 1993-10-12 1996-12-18 壽工業株式会社 Simple waste liquid treatment device

Citations (1)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JPS5259949A (en) * 1975-05-07 1977-05-17 Hitachi Constr Mach Co Ltd Muddy water treating apparatus

Patent Citations (1)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JPS5259949A (en) * 1975-05-07 1977-05-17 Hitachi Constr Mach Co Ltd Muddy water treating apparatus

Also Published As

Publication number Publication date
JPS5410473A (en) 1979-01-26

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