JPS59228916A - Simple treating apparatus of waste water - Google Patents

Simple treating apparatus of waste water

Info

Publication number
JPS59228916A
JPS59228916A JP58102747A JP10274783A JPS59228916A JP S59228916 A JPS59228916 A JP S59228916A JP 58102747 A JP58102747 A JP 58102747A JP 10274783 A JP10274783 A JP 10274783A JP S59228916 A JPS59228916 A JP S59228916A
Authority
JP
Japan
Prior art keywords
tank
sludge
water
waste water
organic chemical
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
JP58102747A
Other languages
Japanese (ja)
Other versions
JPH0442049B2 (en
Inventor
Toshihiko Ito
敏彦 伊藤
Toshio Seki
敏夫 関
Masanori Sadamori
定森 正典
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.)
ICHIKAWA KEORI KK
Ichikawa Woolen Textile Co Ltd
Original Assignee
ICHIKAWA KEORI KK
Ichikawa Woolen Textile 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 ICHIKAWA KEORI KK, Ichikawa Woolen Textile Co Ltd filed Critical ICHIKAWA KEORI KK
Priority to JP58102747A priority Critical patent/JPS59228916A/en
Publication of JPS59228916A publication Critical patent/JPS59228916A/en
Publication of JPH0442049B2 publication Critical patent/JPH0442049B2/ja
Granted legal-status Critical Current

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  • Treatment Of Sludge (AREA)
  • Filtration Of Liquid (AREA)

Abstract

PURPOSE:To obtain the sludge with less water content by arranging organically efficient and small-sized apparatuses, and performing continuously, efficiently, and rapidly the waste water treatment with the compact and efficient apparatuses. CONSTITUTION:The waste water, after flowing into a storage tank 1 and staying therein for a time, is sent to a reaction tank 2. And an acidic inorganic chemical and a basic inorganic chemical are injected respectively from a dissolving tank 3 and a dissolving tank 4 to grow the substance contained in the waste water into larger flocs. Then after the waste water, when needed, is introduced into a flocculator 16 and an organic chemical such as a high molecular flocculant is injected, the waste water contg. flocs is poured ceaselessly into a skimming chamber 6 in a filtration and concentrating apparatus 5. The purified water is discharged, and the water contg. some SS is returned to the storage tank 1. The sludge, after reaching a whipper 12 and being knocked down therefrom, is added in an agitating and mixing tank 13 with an organic chemical such as a high molecular flocculant from an organic chemical dissolving tank 15, and then sent to a dehydrator 17 wherein the water content of the sludge is regulated to <=85%. The treated sludge is dropped into a sludge receiving box 23, and discarded.

Description

【発明の詳細な説明】 本発明は産業廃水、生活廃水など各種の廃水をコンパク
トな機構で連続的に、しかも効率よく迅速に処理し、水
質を良化すると共に含水率の少ない汚泥を得る簡易廃水
処理装置に係り、詳しくは流入する廃水の水質を平均化
する貯留槽と、汚泥のフロイクを形成せしめる反応槽及
びこれに付設した酸性無機薬品溶解槽及び塩基性無機薬
品溶解槽と、生成した70ツクtl−炉水するスキミン
グ室と汚泥排除室よりなる槽及びこの中に傾斜して設け
た無端状の植毛F材で構成された濾過濃縮装置と、濃縮
した汚泥を攪拌し、脱水し易い状態にする半円筒状で上
部が開放している攪拌混合槽及びこれに付設した有機薬
品溶解槽と、プレーンで空胴のシリンダーのプレスロー
ル、ガイドロール及びこれらに接して走行する無端状の
吸水性ベルトよりなる脱水機と、これら諸装置を連絡す
るパイプ等の移送手段により構成されている簡易廃水処
理装置に関するものである。
DETAILED DESCRIPTION OF THE INVENTION The present invention is a method for processing various kinds of wastewater such as industrial wastewater and domestic wastewater continuously, efficiently and quickly using a compact mechanism, improving water quality and easily producing sludge with a low water content. Regarding wastewater treatment equipment, in detail, it includes a storage tank that equalizes the water quality of inflowing wastewater, a reaction tank that forms sludge floes, an acidic inorganic chemical dissolution tank and a basic inorganic chemical dissolution tank attached to this, and A tank consisting of a skimming chamber and a sludge removal chamber for carrying 70 tl of reactor water, a filtration and concentration device consisting of an endless flocked F material installed slanted inside the tank, and a filtration and concentration device that stirs the concentrated sludge and makes it easy to dewater. A semi-cylindrical stirring mixing tank with an open top, an attached organic chemical dissolving tank, a plain hollow cylinder press roll, a guide roll, and an endless water absorber running in contact with these. The present invention relates to a simple wastewater treatment device comprising a dehydrator made of a plastic belt and a transfer means such as a pipe that connects these devices.

従来、廃水を汚泥の生成まで連続的に処理する装置とし
て?−i凝集沈澱処理装置、加圧浮上装置、活性汚泥処
理装置などを一連に設置して順次処理して行くものがあ
るが生物的処理によるため反応速度が遅く、処理効率が
低いため処理に長時間を要した。従って装置は必然的に
大型となる上に犬がかりな土木工事が伴い、更に設置す
るための広大な土地を必要とするので設備コストが莫大
なものとなる。従って経済的にかなりのゆとりがないと
設置が極めて困難で、特に中小規模の事業所では資金が
乏しいので対策に苦慮するのが実状であった。本発明は
これ等の欠点を改良したものであって、土木工事を殆ど
必要としない小型で効率のよい諸装置全有機的に配列し
たコンパクトな構成とし、設置面積が小さい簡易廃水処
理装置であり、以下図面に基づき説明する。
Conventionally, as a device that continuously processes wastewater up to the production of sludge? -i Some systems install a series of coagulation sedimentation treatment equipment, pressure flotation equipment, activated sludge treatment equipment, etc. to perform treatment in sequence, but because they are biological treatments, the reaction speed is slow and the treatment efficiency is low, so the treatment takes a long time. It took time. Therefore, the device is necessarily large-sized, requires extensive civil engineering work, and requires a vast area of land for installation, resulting in an enormous equipment cost. Therefore, it is extremely difficult to install a system unless you have a considerable amount of financial leeway, and the reality is that small and medium-sized businesses, in particular, struggle to take countermeasures because they lack funds. The present invention has improved these drawbacks, and is a simple wastewater treatment device with a small installation area, which has a compact structure in which small and efficient devices are arranged in an organic manner, requiring almost no civil engineering work. , will be explained below based on the drawings.

貯留槽1は公知のものであるが以後の工程の諸装置の処
理効率がよいので、その容量は従来のものより小さくて
よい。この貯留槽で廃水を一時滞留させ、その均一化を
計る。
Although the storage tank 1 is a well-known type, its capacity can be smaller than that of the conventional type because the processing efficiency of various devices in subsequent steps is good. The wastewater is temporarily retained in this storage tank to ensure its uniformity.

反応槽2は文型の槽と、この内部に攪拌機へを備えたも
のであり、該貯留槽とはパイプL1によりポンプP1′
!i−介して連絡しである。該反応槽に近接して立型の
酸、性無機薬品溶解槽3及び塩基性無機薬品溶解槽4が
併設してあり、その各々は攪拌機A2.A3を備え、該
反応槽とパイプL2゜L3によりポンプP2 r P3
を介して連絡しである。
The reaction tank 2 is a sentence-shaped tank and is equipped with a stirrer inside, and the storage tank is connected to a pump P1' by a pipe L1.
! I will contact you via i-. A vertical acidic and basic inorganic chemical dissolving tank 3 and a basic inorganic chemical dissolving tank 4 are installed adjacent to the reaction tank, each of which is equipped with an agitator A2. A3, and pumps P2 r P3 are connected to the reaction tank and pipes L2゜L3.
Please contact us via.

濾過濃縮装置5はスキミング室6と、汚泥排除室7より
なる槽8と、この槽内に傾斜して配置され、断続的に回
転する無端状の植毛炉材9と、これの駆動ロール1oに
連動せしめ、該スキミンク室に設けた7 o −)スイ
ッチ11と、該植毛炉材の下側走行面に接して設けたホ
イツパ−12よりなり、該反応槽とはパイプL4によっ
てポンプP4を介して連続し、該スキミング室の下部は
2つに仕切られ一方は浄化水を受ける部分13aで、パ
イプL5により浄化水排出溝に連なり、他方はSSをや
や含んだ濾過水を受ける部分13bでパイプL6により
該貯留槽に連絡している。
The filtration/concentration device 5 includes a skimming chamber 6, a tank 8 consisting of a sludge removal chamber 7, an endless flocking furnace material 9 that is arranged inclined in the tank and rotates intermittently, and a drive roll 1o for this. It is made up of a 7o-) switch 11 provided in the skimming chamber and a whipper 12 provided in contact with the lower running surface of the flocking furnace material, and is connected to the reaction tank via a pump P4 by a pipe L4. Continuously, the lower part of the skimming chamber is partitioned into two parts, one is a part 13a that receives purified water and is connected to the purified water discharge groove through a pipe L5, and the other part is a part 13b that receives filtrated water slightly containing SS and is connected to a pipe L6. is connected to the storage tank.

攪拌混合槽13は半円筒状で上部が開放している槽でこ
の内部に回転翼14が設けである。該濾過濃縮装置及び
次工程との間にはンユー)sj。
The stirring mixing tank 13 is a semi-cylindrical tank with an open top, and a rotary blade 14 is provided inside the tank. There is no connection between the filtration and concentration device and the next step.

S2が設けである。該攪拌混合槽に近接して有機薬品溶
解槽15が設けられ、その内部には攪拌機A4を備え、
該攪拌混合槽とはパイプL7によりポンプPsk介して
連絡しである。又他の実施例として前記反応槽の次工程
に攪拌機A5を備えた凝集槽16を設け、この有機薬品
混合槽とパイプL8によりポンプP6ヲ介して、又該濾
過濃縮装置とパイプL、によりポンプp71介して連絡
する手段全追加設置することもできる。
S2 is provided. An organic chemical dissolution tank 15 is provided adjacent to the stirring mixing tank, and a stirrer A4 is provided inside the tank.
A pipe L7 communicates with the stirring mixing tank via a pump Psk. As another embodiment, a coagulation tank 16 equipped with an agitator A5 is provided in the next step of the reaction tank, and a pump P6 is connected to this organic chemical mixing tank and pipe L8, and a pump is connected to the filtration concentration device and pipe L. All additional means of communication via p71 can also be installed.

脱水機νはプレーンで空胴のシリンダー18.1乃至2
本のプレスロール19、複数本のガイドロール20及び
これらに接して走行する無端状の吸水性ベルト21によ
シ構成されており該吸水性ベルトは合成繊維入ガ又は天
然111!祿よフなる織フェルト、ニードルフェルト又
は植毛布よりなっており、この吸水性ベルトが該シリン
ダー通過後の反転部分には汚泥掻き取りナイフ22が備
えてあり、この下方には汚泥量は箱23が設けである。
The dehydrator ν is a plain hollow cylinder 18.1 to 2.
It is composed of a book press roll 19, a plurality of guide rolls 20, and an endless water absorbent belt 21 running in contact with these. The absorbent belt is made of woven felt, needle felt, or flocked cloth, and a sludge scraping knife 22 is provided at the inverted part after the water-absorbing belt passes through the cylinder, and a box 23 for measuring the amount of sludge is provided below this. is the provision.

この脱水機と該貯留槽間はパイプL、。で連絡されてい
て濾過水を返送するようになっている。
A pipe L is connected between this dehydrator and the storage tank. have been contacted and the filtered water will be sent back.

次にこの装置を用いた作用を説明する。廃水は先ず貯留
槽1に流入し、ここで一時滞留し、水質が略々均一にな
る。
Next, the operation using this device will be explained. The wastewater first flows into the storage tank 1, where it temporarily stagnates, and the water quality becomes approximately uniform.

次にポンプP1によりパイプL+ f通して反応槽2に
送る。一方予め溶解して置いた硫酸アルミニウムの如き
酸性無機薬品をその溶解槽3より注入し、攪拌機A1で
攪拌すると廃水中の含有物質は金属の水酸化物の錯イオ
ンとなり、これにBODの要素となる亜コロイド及びコ
ロイドが吸着した70ツクが形成される。更にこれも予
め溶解しておいた水酸化ナトリウムの如き塩基性無機薬
品をその溶解槽4より注入し攪拌すると速い反応速度で
水不溶性の金属の水酸化物となって大きなフロックに成
長する。かかる処理水を更に必要に応じて凝集槽16に
導入し、予め溶解しておいた高分子凝集剤の如き有機薬
品を注入し、攪拌機A5で攪拌して直径50μ以上のフ
ロックに成長せしめる。
Next, it is sent to the reaction tank 2 through the pipe L+f by the pump P1. On the other hand, when pre-dissolved acidic inorganic chemicals such as aluminum sulfate are injected from the dissolution tank 3 and stirred by the stirrer A1, the substances contained in the wastewater become complex ions of metal hydroxides, which are combined with elements of BOD. 70 pieces of subcolloids and colloids are formed. Furthermore, when a pre-dissolved basic inorganic chemical such as sodium hydroxide is poured into the dissolving tank 4 and stirred, it becomes a water-insoluble metal hydroxide at a high reaction rate and grows into a large floc. The treated water is further introduced into the flocculation tank 16 as required, and a pre-dissolved organic chemical such as a polymer flocculant is injected thereinto, and stirred by the stirrer A5 to grow flocs with a diameter of 50 μm or more.

次にこのフロックを含有した廃水ti過濃縮装置漫のス
キミング室6に間断なく注ぐ。植毛炉材9は目詰りが少
ないうちは停止しているが濾過が進み、汚泥の附着が多
くなると水位が上昇し、フロートスイッチ11が作動し
て該植毛炉材が進行し、附着した汚泥はホイツパ−12
の所に至って叩き落される。該植毛炉材の清浄部分が上
側走行部に現れると濾過が進み水位が低下して該植毛炉
材は停止する。かかる作用が繰返される。浄化水は放流
し、若干のss’l含有した水は貯留槽1に返送される
。叩き落された汚泥はンユートS、を滑降して攪拌混合
槽13に入り、有機薬品溶解槽15よジ高分子凝集剤の
如き有機薬品が加えられ、回転翼14で攪拌すると塊状
の汚泥が細分し、粒状化して脱水し易い状態となる。こ
の粒状汚泥はシュートs2を滑降して脱水機υの無端状
の吸水性ベルト21上に落下し、送られて/リンダー1
8に至り、プレスロール19の加圧及び該吸水性ベルト
の押圧力により脱水され、含水率85%以下の汚泥とな
り、掻き取りナイフ22で掻き落され、汚泥受は箱23
に落下し、廃棄される。濾過水は貯留槽1に返送される
Next, the wastewater containing this floc is continuously poured into the skimming chamber 6 of the superconcentrator. The flocking furnace material 9 is stopped while there is little clogging, but as filtration progresses and more sludge adheres, the water level rises, the float switch 11 is activated, the flocking furnace material advances, and the adhered sludge is removed. Whizpa-12
When he reached the place, he was knocked down. When the clean part of the flocking furnace material appears on the upper running section, filtration progresses, the water level decreases, and the flocking furnace material stops. This action is repeated. The purified water is discharged, and the water containing some ss'l is returned to the storage tank 1. The knocked-off sludge slides down the unit S and enters the stirring mixing tank 13, where an organic chemical such as a polymer flocculant is added to the organic chemical dissolving tank 15, and when stirred by the rotary blades 14, the lumpy sludge is broken down into small pieces. However, it becomes granular and easily dehydrated. This granular sludge slides down the chute s2, falls onto the endless water-absorbing belt 21 of the dehydrator υ, and is sent to the linder 1.
8, the water is dehydrated by the pressurization of the press roll 19 and the pressing force of the water-absorbing belt, resulting in sludge with a water content of 85% or less, which is scraped off with the scraping knife 22, and the sludge receiver is placed in the box 23.
It falls and is discarded. The filtered water is returned to the storage tank 1.

以上のように本発明の簡易廃水処理装置は効率のよい小
型の諸装置を有機的に配設したコンパクトで効率のよい
装置であり、廃水の処理を連続的に効率よく迅速に行い
含水率が極めて少ない汚泥全書るので廃棄が容易であり
、且つ処理後の放流水のSS含有量、BoD値などは極
めて少なく、水質が向上し、又コンパクトであるから安
価で、設置が簡単であり、且つ設置面積が小さいなど多
くの利点がある。
As described above, the simple wastewater treatment device of the present invention is a compact and efficient device that organically arranges efficient small-sized devices, and it processes wastewater continuously, efficiently and quickly, and reduces the water content. It is easy to dispose of because it produces only a very small amount of sludge, and the SS content and BoD value of the effluent after treatment are extremely low, improving water quality.It is also compact, making it inexpensive and easy to install. It has many advantages, including a small footprint.

次に本発明の装置により処理した実施例を述べる。Next, we will describe an example of processing using the apparatus of the present invention.

実施例1゜ 洗米廃水で流入量が20ovrty日で原水の水質がP
H−6,0〜7.O5S=600〜700ppm BO
D=700〜800ppmのものを処理したところ、放
流水はPH=6.5SS=49ppm BOD=46p
pm、汚泥の含水率は83%となり、ランニング処理コ
ストハフ0円/77/で、設置面積は従来の活性汚泥処
理システムの勿であった。父上記IN、量の処理に要し
た時間は8時間であり、従来法では24時間を要した。
Example 1゜Rice washing wastewater has an inflow of 20 ovrty days and the raw water quality is P.
H-6, 0-7. O5S=600~700ppm BO
When D=700-800ppm was treated, the effluent water was PH=6.5SS=49ppm BOD=46p
pm, the water content of the sludge was 83%, the running treatment cost was 0 yen/77/h, and the installation area was comparable to that of conventional activated sludge treatment systems. The time required to process the above IN amount was 8 hours, compared to 24 hours using the conventional method.

実施例2 公共施設の焼却炉の洗煙及び洗灰廃水を本発明の装置で
処理したところ安定したフロックを得、最終汚泥の含水
率は65%であった。
Example 2 When smoke and ash washing wastewater from an incinerator in a public facility was treated with the apparatus of the present invention, stable flocs were obtained, and the moisture content of the final sludge was 65%.

濾過水は一旦タラリファイヤーに滞留させ、沈降分離を
促進し、水質の安定、向上を計り洗滌水に再利用した。
The filtered water was temporarily retained in the talarifier to promote sedimentation and separation, stabilize and improve water quality, and reuse it as washing water.

従来の洗煙及び洗灰方法では廃水の性状の変動が極めて
大きく、薬品処理後のタラリファイヤーにおける沈降性
が悪く、再利用し得る水質にならず、殆どキャリオーバ
ーしていた。
In conventional smoke washing and ash washing methods, the properties of the wastewater fluctuate significantly, and the sedimentation properties in the talarifier after chemical treatment are poor, resulting in poor water quality that can be reused and almost carryover.

実施例3 水産加工業の鯖ぶし作業における煮汁の廃水処理を本発
明の装置で行った。原水の水質はPH=7.O5S=5
00−8[1[]ppm  BOD=5[110〜T0
,000ppmであった。薬品の注入は無機薬品として
硫酸アルミニウム、水酸化ナト1ノウムを、有機薬品と
してポリアクリルアミド全加えた。処理後の汚泥の含水
率は785Xで肥料に活用した。
Example 3 Wastewater treatment of broth from mackerel processing in the seafood processing industry was carried out using the apparatus of the present invention. The quality of raw water is PH=7. O5S=5
00-8[1[]ppm BOD=5[110~T0
,000ppm. When injecting chemicals, aluminum sulfate and sodium hydroxide were added as inorganic chemicals, and polyacrylamide was added as an organic chemical. The water content of the sludge after treatment was 785X and was used as fertilizer.

2i5過水はPJ(=/)、813fa=80ppm 
BOD=70pprnとなり問題なく放流した。
2i5 superhydration is PJ (=/), 813fa=80ppm
The BOD was 70 pprn and discharged without any problem.

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

Claims (2)

【特許請求の範囲】[Claims] (1)  流入する廃水の水質を平均化する貯留槽と、
汚泥の70ツクを形成せしめる反応槽及びこれに付設し
た酸性無機薬品溶解槽及び塩基性無機薬品溶解槽と、生
成したフロックを炉水するスキミング室と汚泥排除室よ
りなる槽及びこの中に傾斜して設けた無端状の植毛Fp
で構成された濾過濃縮装置と、濃縮した汚泥を攪拌し、
脱水し易い状態にする半円筒状で上部が開放している攪
拌混合槽及びこれに付設した有機薬品溶解槽と、プレー
ンで空胴のシリンター、プレスロール、カイトロール、
及びこれらに接して走行する無端状の吸水性ベルトより
なる脱水機と、これら諸装置を連絡するパイプ等の移送
手段により構成されていることを特徴とする簡易廃水処
理装置。
(1) A storage tank that equalizes the quality of inflowing wastewater;
A reaction tank for forming 70 tons of sludge, an attached acidic inorganic chemical dissolving tank and a basic inorganic chemical dissolving tank, a tank consisting of a skimming room and a sludge removal room for discharging the generated flocs with reactor water; Endless flocked Fp provided with
A filtration and concentration device consisting of
A semi-cylindrical stirring mixing tank with an open top that facilitates dehydration, an attached organic chemical dissolving tank, a plain hollow cylinder, a press roll, a kite roll,
A simple wastewater treatment device comprising: a dehydrator made of an endless water-absorbing belt that runs in contact with these devices; and a transfer means such as a pipe that connects these devices.
(2)該反応槽の次工程に凝集槽を配置し、且つ該有機
薬品溶解槽とパイプにより連絡したことを特徴とする特
許請求の範囲第(1)項記載の簡易廃水処理装置。
(2) The simple wastewater treatment device according to claim (1), characterized in that a coagulation tank is disposed in a step subsequent to the reaction tank, and is connected to the organic chemical dissolution tank by a pipe.
JP58102747A 1983-06-10 1983-06-10 Simple treating apparatus of waste water Granted JPS59228916A (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
JP58102747A JPS59228916A (en) 1983-06-10 1983-06-10 Simple treating apparatus of waste water

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
JP58102747A JPS59228916A (en) 1983-06-10 1983-06-10 Simple treating apparatus of waste water

Publications (2)

Publication Number Publication Date
JPS59228916A true JPS59228916A (en) 1984-12-22
JPH0442049B2 JPH0442049B2 (en) 1992-07-10

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Family Applications (1)

Application Number Title Priority Date Filing Date
JP58102747A Granted JPS59228916A (en) 1983-06-10 1983-06-10 Simple treating apparatus of waste water

Country Status (1)

Country Link
JP (1) JPS59228916A (en)

Cited By (1)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JP2002292400A (en) * 2001-04-02 2002-10-08 Nippon Steel Corp Dehydration equipment for low concentration slurry

Citations (2)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JPS5117071A (en) * 1974-08-01 1976-02-10 Iwao Kogyo Kk Suichukendakubutsuo jokyosuruhoho
JPS5328298U (en) * 1976-08-13 1978-03-10

Patent Citations (2)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JPS5117071A (en) * 1974-08-01 1976-02-10 Iwao Kogyo Kk Suichukendakubutsuo jokyosuruhoho
JPS5328298U (en) * 1976-08-13 1978-03-10

Cited By (2)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JP2002292400A (en) * 2001-04-02 2002-10-08 Nippon Steel Corp Dehydration equipment for low concentration slurry
JP4688332B2 (en) * 2001-04-02 2011-05-25 新日鉄エンジニアリング株式会社 Low concentration slurry dewatering equipment

Also Published As

Publication number Publication date
JPH0442049B2 (en) 1992-07-10

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