JPH0233440B2 - - Google Patents
Info
- Publication number
- JPH0233440B2 JPH0233440B2 JP56074676A JP7467681A JPH0233440B2 JP H0233440 B2 JPH0233440 B2 JP H0233440B2 JP 56074676 A JP56074676 A JP 56074676A JP 7467681 A JP7467681 A JP 7467681A JP H0233440 B2 JPH0233440 B2 JP H0233440B2
- Authority
- JP
- Japan
- Prior art keywords
- air
- porous
- air diffuser
- porous plate
- diffuser
- 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
Links
Classifications
-
- Y—GENERAL TAGGING OF NEW TECHNOLOGICAL DEVELOPMENTS; GENERAL TAGGING OF CROSS-SECTIONAL TECHNOLOGIES SPANNING OVER SEVERAL SECTIONS OF THE IPC; TECHNICAL SUBJECTS COVERED BY FORMER USPC CROSS-REFERENCE ART COLLECTIONS [XRACs] AND DIGESTS
- Y02—TECHNOLOGIES OR APPLICATIONS FOR MITIGATION OR ADAPTATION AGAINST CLIMATE CHANGE
- Y02W—CLIMATE CHANGE MITIGATION TECHNOLOGIES RELATED TO WASTEWATER TREATMENT OR WASTE MANAGEMENT
- Y02W10/00—Technologies for wastewater treatment
- Y02W10/10—Biological treatment of water, waste water, or sewage
Landscapes
- Aeration Devices For Treatment Of Activated Polluted Sludge (AREA)
- Nozzles (AREA)
Description
【発明の詳細な説明】
本発明は、産業排水やシ尿等の高濃度廃水をは
じめとする汚水処理に用いる散気装置に関する。DETAILED DESCRIPTION OF THE INVENTION The present invention relates to an aeration device used for treating sewage including highly concentrated wastewater such as industrial wastewater and human urine.
一般に下水や排水等の汚水は活性汚泥曝気槽に
貯水され、該曝気槽内に沈設された散気装置か
ら、噴射された空気により、活性汚泥に付着した
汚水中の汚濁物質を、栄養源として前記活性汚泥
に吸収酸化せしめることで浄化処理がなされてい
る。 Generally, wastewater such as sewage and wastewater is stored in an activated sludge aeration tank, and air is injected from an aeration device installed in the aeration tank to convert pollutants in the sewage that have adhered to the activated sludge into nutrients. Purification treatment is performed by absorbing and oxidizing the activated sludge.
第1図は、かかる従来の散気装置の断面図であ
る。図中、1は散気部、2は多数の小孔3が形成
された多孔質板、4は枝管であり、図示しないコ
ンプレツサーに一端が接続された送気管に連通し
ており、該枝管4に形成した穴部4aには散気部
1の根元部1aが組み込まれている。 FIG. 1 is a sectional view of such a conventional air diffuser. In the figure, 1 is an air diffuser, 2 is a porous plate in which many small holes 3 are formed, and 4 is a branch pipe, which communicates with an air supply pipe whose one end is connected to a compressor (not shown). The root portion 1a of the air diffuser 1 is incorporated into the hole 4a formed in the tube 4.
前記多孔質板2の小孔3は、該小孔3の直径が
100乃至400μm程度で比較的大きいため、汚濁物
質が該小孔3内部に侵入し目づまりを起し易く、
再使用が不可能になり易い欠点があつた。しかも
該目づまりを防止するために、コンプレツサーよ
り多孔質板2へ送る単位面積あたりの風量を、
100ml/min・cm2以上にしなければならず、この
風量では気泡の分散性を低め且つ大型コンプレツ
サーを必要とするので大量の電力を消費するた
め、近年の省エネルギーに相反するものであつ
た。さらに前記100ml/min・cm2以上の風量のも
とでは、前記小孔3より散気すると、一つの小か
ら出た気泡5aと該小孔に隣接する他の小孔から
出た気泡5bとが併合して、大きな気泡5cを形
成するいわゆる合泡現象を生じ易い。この合泡現
象が生じると理想の微細気泡を発生できず、汚濁
物質の浄化に利用される酸素の割合、即ち酸素溶
解効率が低下し、高々10%未満となり効率の良い
汚水処理を行なうことができない。又、多孔質板
2は単層に形成されているので、耐久性を保持し
且つ微細気泡を得るためには、該多孔質板の厚み
を相当厚くしなければならず、その結果ブロアに
多大なエネルギーロスを生じる。 The small holes 3 of the porous plate 2 have a diameter of
Since it is relatively large at about 100 to 400 μm, it is easy for pollutants to enter the inside of the small hole 3 and cause clogging.
It had the disadvantage that it was likely to be impossible to reuse. Moreover, in order to prevent clogging, the air volume per unit area sent from the compressor to the porous plate 2 is
The air volume must be 100 ml/min·cm 2 or more, and this air volume reduces the dispersion of air bubbles and requires a large compressor, which consumes a large amount of electricity, which is contrary to recent energy conservation efforts. Furthermore, under the air volume of 100 ml/min・cm 2 or more, when air is diffused from the small hole 3, the air bubbles 5a coming out of one small hole and the air bubbles 5b coming out from another small hole adjacent to the small hole are separated. A so-called coalescence phenomenon in which large bubbles 5c are formed is likely to occur. When this bubbling phenomenon occurs, the ideal microbubbles cannot be generated, and the proportion of oxygen used to purify pollutants, that is, the oxygen dissolution efficiency, decreases and becomes less than 10% at most, making it difficult to carry out efficient wastewater treatment. Can not. In addition, since the porous plate 2 is formed in a single layer, the thickness of the porous plate must be made considerably thick in order to maintain durability and obtain fine bubbles, and as a result, the blower requires a large amount of thickness. This causes significant energy loss.
以上から本発明は、散気装置の目づまりを防止
できると共に電力消費量を低減でき、しかも合泡
現象を無くせ、更には耐久性を維持しながら圧力
損失を低減せしめる散気装置を提供することを目
的とする。 From the above, it is an object of the present invention to provide an air diffuser that can prevent clogging of the air diffuser, reduce power consumption, eliminate the bubbling phenomenon, and further reduce pressure loss while maintaining durability. purpose.
以下、本発明の一実施例を図面をもちいて詳細
に説明する。 Hereinafter, one embodiment of the present invention will be described in detail with reference to the drawings.
第2図は汚水処理装置の断正面図、第3図は本
発明による散気部の断側面図、第4図は散気部内
における空気の通過過程を示す断面図、第5図は
保護用ネツトの正面図である。 Fig. 2 is a sectional front view of the sewage treatment equipment, Fig. 3 is a sectional side view of the aeration section according to the present invention, Fig. 4 is a sectional view showing the passage process of air in the aeration section, and Fig. 5 is for protection. It is a front view of the net.
第2図において、11は曝気槽で該曝気槽11
内には活性汚泥及び汚濁物水溶液等の混合液体1
2が貯えられている。13は曝気槽11内の底部
に沈設された散気装置で、コンプレツサー14に
より加圧された空気が、送気管15を通つて圧送
される。尚、送気管15を通つて圧送されてきた
空気は、該送気管に接続された集合管16及び該
集合管16より導出した枝管17を介して散気部
18に至り、該散気部表面より気泡流となつて前
記混合液体12内に噴射される。 In FIG. 2, 11 is an aeration tank.
Inside is a mixed liquid such as activated sludge and pollutant aqueous solution 1
2 are stored. Reference numeral 13 denotes an aeration device installed at the bottom of the aeration tank 11, through which air pressurized by a compressor 14 is sent under pressure through an air supply pipe 15. Note that the air that has been pressure-fed through the air supply pipe 15 reaches the air diffuser 18 via a collecting pipe 16 connected to the air pipe and a branch pipe 17 led out from the collecting pipe 16, and then reaches the air diffuser 18. The bubbles are injected from the surface into the mixed liquid 12.
第3図は、本発明による散気装置の拡大断側面
図であり、図中散気部18は、断面形状が上に開
いた漏斗状を成し、その根元部にはチエツキバル
ブ19が設けてある。該チエツキバルブ19は、
矢印A方向への空気の流出は許容するも、逆矢印
A′方向からの水流の流入を防止するためのもの
で、一般にはゴム材等より成り、バネ20により
矢印A′方向にバイアスされている。21は、キ
ヤツプ部で後述する複数枚の多孔質板を該キヤツ
プ部内部に把持すると共に散気部18の本体にネ
ジ止め可能に設けてあり、一方の端部には円形状
のフランジ22が、他方の端部には複数個の抜け
防止部材23…が設けてある。24は平板状の第
一の多孔質体である。該多孔質板24はプラスチ
ツク等の多孔質で樹脂の粉末、たとえばポリアミ
ド樹脂、ポリエチレン樹脂、ポリプロピレン樹
脂、塩化ビニール樹脂、ACS樹脂等の熱可塑性
樹脂の粉末を平板状に圧縮成形後、該圧縮成形品
を型に入れたまま窒素ガス等の不活性雰囲気中に
約250℃にて約30分間焼成したもので、第4図に
示すように細かい無数の小孔24a…を備えてい
る。25は前記第1の多孔質板24上に配設した
第2の多孔質板である。該第2の多孔質板25も
前記第1の多孔質板24と同様に製造されるもの
であるが、該第2の多孔質板25は、その製造前
の樹脂の粉末を前記第1の多孔質板24より細か
くしたものである。従つて製造された第2の多孔
質板25は、第1の多孔質板24より細かい無数
の小孔25a…を有するものである。 FIG. 3 is an enlarged cross-sectional side view of the air diffuser according to the present invention. In the figure, the air diffuser 18 has a funnel-shaped cross section that opens upward, and a check valve 19 is provided at the base of the air diffuser 18. be. The check valve 19 is
Allowing air to flow in the direction of arrow A, but in the opposite direction
This is to prevent water flow from flowing in from the direction A', and is generally made of a rubber material or the like, and is biased in the direction of the arrow A' by a spring 20. Reference numeral 21 is a cap portion that holds a plurality of porous plates, which will be described later, inside the cap portion, and is provided so as to be screwable to the main body of the air diffuser 18, and a circular flange 22 is provided at one end. , a plurality of slip-off prevention members 23 are provided at the other end. 24 is a flat plate-shaped first porous body. The porous plate 24 is made of porous resin such as plastic, for example, after compression molding powder of thermoplastic resin such as polyamide resin, polyethylene resin, polypropylene resin, vinyl chloride resin, ACS resin, etc. into a flat plate shape, the compression molding is performed. The product is baked in an inert atmosphere such as nitrogen gas at about 250°C for about 30 minutes while still in the mold, and has numerous fine holes 24a as shown in Figure 4. 25 is a second porous plate disposed on the first porous plate 24. The second porous plate 25 is also manufactured in the same manner as the first porous plate 24, but the second porous plate 25 is made by mixing the resin powder before manufacturing with the first porous plate 25. It is made finer than the porous plate 24. The second porous plate 25 thus produced has numerous small holes 25a that are smaller than the first porous plate 24.
26は、第2の多孔質板25上を配設した第3
の多孔質板である。該多孔質板26も前記各多孔
質板24,25と同様に製造されるも、その製造
前の樹脂粉末を第2の多孔質板25のそれよりも
さらに細かくしたものである。従つて、第3の多
孔質板26は第2の多孔質板25よりさらに細か
い無数の小孔26a…を有する。27は、第3の
多孔質板26上に配設した多孔質材よりなる不織
布で、該不織布27の一面(散気表面)にはフツ
素樹脂膜28がコーテイングされてある。なお、
前記フツ素樹脂膜28には第4図に示すように細
かい無数の約3乃至5μm程度の小孔28a…が設
けてある。29は散気表面保護用のネツトであ
り、このネツトは第5図イに示すように十文字状
に形成されている。尚、このネツトは第5図ロ,
ハに示すように、丸にI字状に設けてもよい。 26 is a third porous plate disposed on the second porous plate 25;
It is a porous board. Although the porous plate 26 is manufactured in the same manner as the porous plates 24 and 25, the resin powder before manufacture is made finer than that of the second porous plate 25. Therefore, the third porous plate 26 has numerous small holes 26a that are smaller than the second porous plate 25. Reference numeral 27 denotes a nonwoven fabric made of a porous material disposed on the third porous plate 26, and one surface (diffusing surface) of the nonwoven fabric 27 is coated with a fluororesin film 28. In addition,
As shown in FIG. 4, the fluororesin film 28 is provided with countless small holes 28a of approximately 3 to 5 μm in size. 29 is a net for protecting the air diffuser surface, and this net is formed in a cross shape as shown in FIG. 5A. In addition, this net is shown in Figure 5 B,
As shown in FIG. 3, it may be provided in an I-shape in a circle.
さて、前記した多孔質板24,25,26、不
織布27を散気部18に内設するには、本体より
キヤツプ部21を外し、該キヤツプ部のフランジ
22側に順次、ネツト29、不織布27、第3、
第2の多孔質板26,25を収納し、最後に第1
の多孔質板24を内設し、複数個の抜け防止部材
23…に係止させればよい。この時、抜け防止部
材23…はフランジ22側に向つて徐々に突出し
た傾斜面をなつているため、多孔質板の装着作業
は簡単で且つ、簡単には抜けることはない。その
後、キヤツプ部21を本体にネジ止めすればよい
ものである。 Now, in order to install the above-mentioned porous plates 24, 25, 26 and non-woven fabric 27 inside the air diffuser 18, remove the cap part 21 from the main body, and sequentially install the net 29, non-woven fabric 27 on the flange 22 side of the cap part. , third,
The second porous plates 26 and 25 are stored, and finally the first
A porous plate 24 may be provided therein, and the plurality of slip-out prevention members 23 may be engaged with the porous plate 24. At this time, since the falling-off preventing members 23 have sloped surfaces that gradually protrude toward the flange 22, the porous plate can be easily attached and will not easily fall off. Thereafter, the cap portion 21 may be screwed onto the main body.
そして、枝管17より搬送された空気はチエツ
キバルブ19を押圧し、散気部18の空気室18
a内に流入し、その後、各多孔質板24,25,
26、不織布27、フツ素樹脂膜28を径由して
小さな気泡流となつて混合板12内に噴射される
ものである。 Then, the air conveyed from the branch pipe 17 presses the check valve 19, and the air chamber 18 of the air diffuser 18
a, and then each porous plate 24, 25,
26, the nonwoven fabric 27, and the fluororesin film 28, and are injected into the mixing plate 12 as a small bubble flow.
そこで前記気泡流になる状態について第3図及
び第4図を用いて説明すると、空気室18a(第
3図)内に流入した空気は先づ第1の多孔質板2
4の小孔24aに通過する過程で小さな気泡にさ
れる。その気泡は第2の多孔質板25の小孔25
aによりさらに小さい気泡とされ、さらに第3の
多孔質板26の小孔26aによりさらに小さい気
泡となる。そして最後に不織布27、フツ素樹脂
膜28の小孔28aより噴射されるものであり、
この時気泡は前記各多孔質板24,25,26を
通過する過程で、徐々に細微化されるため、空気
(気泡)の分散性がよく、気泡は従来のような合
泡現象を発生することはない。 Therefore, to explain the state of the bubble flow using FIGS. 3 and 4, the air flowing into the air chamber 18a (FIG. 3) first flows through the first porous plate 2.
In the process of passing through the small hole 24a of No. 4, it becomes small bubbles. The air bubbles are formed in the small holes 25 of the second porous plate 25.
The bubbles are made even smaller by the small holes 26a of the third porous plate 26. Finally, it is sprayed from the small holes 28a of the nonwoven fabric 27 and the fluororesin film 28.
At this time, as the air bubbles pass through each of the porous plates 24, 25, and 26, they are gradually atomized, so that the air (air bubbles) has good dispersibility, and the air bubbles generate a coalescence phenomenon as in the conventional case. Never.
また、散気部18(第3図)への空気の流入が
停止しても、フツ素樹脂膜28表面に付着した汚
濁物質は、該膜28に設けた小孔28aが非常な
微細孔であるため、内部に侵入することはなく、
目づまりを生じない。また該微細孔内部に侵入す
るものは、完全にろ過された清水に近いものであ
り、該清水は本散気装置において何ら支障をきた
すものではない。さらに膜28に付着した汚濁物
質は再び気泡Bが噴射された時、該気泡により簡
単に剥離するものである。 Further, even if the inflow of air into the air diffuser 18 (Fig. 3) is stopped, the pollutants adhering to the surface of the fluororesin membrane 28 will be removed due to the small holes 28a provided in the membrane 28 being very fine. Because there is no intrusion inside,
Does not cause clogging. Further, what enters the inside of the micropores is close to completely filtered fresh water, and this fresh water does not cause any trouble in the present air diffuser. Further, the pollutants attached to the membrane 28 are easily peeled off by the bubbles when the bubbles B are injected again.
以上、この発明によれば、散気槽内に存在する
汚濁物質の侵入を防止する機能を果す10μm以下
の小孔径の多孔性の膜を設けて、合泡現象を無く
しかつ電力消費量を高めることなく、酸素溶解効
率を高めて汚水処理を行なうことができる散気装
置を提供できる。従つて前記従来例よりも、極小
な微細気泡を発生でき、これによりコンプレツサ
ーより送られる空気が100ml/min・cm2以下の風
量でも使用可能であり、そのため気泡の分散性を
高め前記酸素溶解効率を倍以上にできる飛躍的成
果をもたらすことができる。また散気部18への
空気流入を停止しても汚濁物質12は、フツ素樹
脂膜28に設けて小孔が極めて微細なために、該
散気部18内部に侵入することはない。さらに該
散気部表面に付着した汚濁物質には、再び気泡流
Oが噴射された時、その分散性により簡単に剥離
する等多大な効果を有するものである。 As described above, according to the present invention, a porous membrane with a small pore size of 10 μm or less is provided, which functions to prevent the intrusion of pollutants present in the air diffuser tank, thereby eliminating the bubbling phenomenon and increasing power consumption. Therefore, it is possible to provide an aeration device that can perform wastewater treatment while increasing oxygen dissolution efficiency. Therefore, it is possible to generate extremely small microbubbles compared to the conventional example, and as a result, the air sent from the compressor can be used even at an air flow rate of 100ml/min・cm 2 or less, which improves the dispersibility of the bubbles and improves the oxygen dissolution efficiency. It can bring about dramatic results that can more than double the amount. Further, even if the air flow into the air diffuser 18 is stopped, the pollutants 12 will not enter the air diffuser 18 because the small holes provided in the fluororesin membrane 28 are extremely fine. Furthermore, when the air bubbles O are again injected onto the pollutants adhering to the surface of the air diffuser, they can be easily peeled off due to their dispersibility, which has a great effect.
また前記目づまりによる弊害を完全除去し且つ
気泡の分散特性に優れているので、シ尿や産業排
水等高濃度廃水に格段の威力を発輝し、しかも消
費電力が安価にできる等多大な効果を有するもの
である。 In addition, it completely eliminates the harmful effects caused by clogging and has excellent bubble dispersion properties, so it is extremely effective for treating highly concentrated wastewater such as human urine and industrial wastewater, and has great effects such as reducing power consumption. It has the following.
第1図は従来例を示す断側面図である。第2図
乃至第5図は、本発明の1実施例を示し、第2図
は汚水処理装置の断正面図、第3図は散気部18
を示す拡大断側面図、第4図は空気の通過過程を
示す要部断側面図、第5図は保護用ネツトであ
る。
図において、13は散気装置、18は散気部、
24,25,26は多孔質板、24a,25a,
26aは小孔、27は不織布、28はフツ素樹脂
膜、28aは小孔である。
FIG. 1 is a sectional side view showing a conventional example. 2 to 5 show one embodiment of the present invention, FIG. 2 is a sectional front view of the sewage treatment equipment, and FIG. 3 is a diffuser 18.
FIG. 4 is an enlarged sectional side view showing the passage of air, and FIG. 5 is a sectional side view of the main part showing the air passage process. In the figure, 13 is an air diffuser, 18 is an air diffuser,
24, 25, 26 are porous plates, 24a, 25a,
26a is a small hole, 27 is a nonwoven fabric, 28 is a fluororesin film, and 28a is a small hole.
Claims (1)
該空気を前記多孔質板の小孔を通過せしめて、前
記散気部から散気槽内に微細気泡を生成する散気
装置において、前記散気部は複数枚の多孔質板を
有し、これら各多孔質板の小孔径は、空気流入側
の多孔質板の平均小孔径より空気流出側に向つて
配置された多孔質板の平均小孔径を小さく形成
し、かつこれら多孔質板は順次間隔をおいて配設
せしめられるとともに、空気流出側の最先端に位
置する多孔質板の散気表面側は、前記散気槽内に
存在する汚濁物質の侵入を防止する10μm以下の
小孔径の多孔性の膜で覆われていることを特徴と
する散気装置。 2 散気表面の多孔性の膜を、不織布とその表面
を覆うフツ素樹脂膜で形成せしめたことを特徴と
する特許請求の範囲第1項記載の散気装置。[Claims] 1. Air is forced into a diffuser section that includes a porous plate,
In the air diffuser which causes the air to pass through the small holes of the porous plate to generate fine bubbles from the air diffuser in the air diffuser tank, the air diffuser has a plurality of porous plates, The pore diameter of each of these porous plates is such that the average pore diameter of the porous plates arranged toward the air outflow side is smaller than the average pore diameter of the porous plates on the air inflow side, and these porous plates are arranged in order. The aeration surface side of the porous plate, which is arranged at intervals and located at the most extreme point on the air outflow side, has small pores with a diameter of 10 μm or less to prevent the entry of pollutants present in the aeration tank. An air diffuser characterized by being covered with a porous membrane. 2. The air diffuser according to claim 1, wherein the porous membrane on the air diffuser surface is formed of a nonwoven fabric and a fluororesin film covering the surface of the nonwoven fabric.
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| JP56074676A JPS57190697A (en) | 1981-05-18 | 1981-05-18 | Air diffusion apparatus |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| JP56074676A JPS57190697A (en) | 1981-05-18 | 1981-05-18 | Air diffusion apparatus |
Publications (2)
| Publication Number | Publication Date |
|---|---|
| JPS57190697A JPS57190697A (en) | 1982-11-24 |
| JPH0233440B2 true JPH0233440B2 (en) | 1990-07-27 |
Family
ID=13554065
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| JP56074676A Granted JPS57190697A (en) | 1981-05-18 | 1981-05-18 | Air diffusion apparatus |
Country Status (1)
| Country | Link |
|---|---|
| JP (1) | JPS57190697A (en) |
Cited By (1)
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|---|---|---|---|---|
| JPWO2025069563A1 (en) * | 2023-09-29 | 2025-04-03 |
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| EP2900356A1 (en) | 2012-09-27 | 2015-08-05 | Evoqua Water Technologies LLC | Gas scouring apparatus for immersed membranes |
| EP3052221B1 (en) | 2013-10-02 | 2022-12-14 | Rohm & Haas Electronic Materials Singapore Pte. Ltd | Device for repairing a membrane filtration module |
| WO2017011068A1 (en) | 2015-07-14 | 2017-01-19 | Evoqua Water Technologies Llc | Aeration device for filtration system |
| JP7150521B2 (en) * | 2017-08-23 | 2022-10-11 | 積水化学工業株式会社 | SEAT STRUCTURE, WASTE WATER TREATMENT APPARATUS INCLUDING THE SAME, AND METHOD FOR MANUFACTURING SEAT STRUCTURE |
| KR102575663B1 (en) * | 2021-04-02 | 2023-09-06 | 김의진 | Micro bubble wastewater treatment apparatus with biofilm |
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Family Cites Families (1)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| JPS632154Y2 (en) * | 1981-03-14 | 1988-01-20 |
-
1981
- 1981-05-18 JP JP56074676A patent/JPS57190697A/en active Granted
Cited By (1)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| JPWO2025069563A1 (en) * | 2023-09-29 | 2025-04-03 |
Also Published As
| Publication number | Publication date |
|---|---|
| JPS57190697A (en) | 1982-11-24 |
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