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JPH0132812B2 - - Google Patents
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JPH0132812B2 - - Google Patents

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Publication number
JPH0132812B2
JPH0132812B2 JP1016181A JP1016181A JPH0132812B2 JP H0132812 B2 JPH0132812 B2 JP H0132812B2 JP 1016181 A JP1016181 A JP 1016181A JP 1016181 A JP1016181 A JP 1016181A JP H0132812 B2 JPH0132812 B2 JP H0132812B2
Authority
JP
Japan
Prior art keywords
copper
dicarboxylate
precipitate
aqueous solution
terephthalate
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
JP1016181A
Other languages
Japanese (ja)
Other versions
JPS57126449A (en
Inventor
Nobuyuki Higozaki
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.)
Juki Corp
Original Assignee
Tokyo Juki Industrial 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 Tokyo Juki Industrial Co Ltd filed Critical Tokyo Juki Industrial Co Ltd
Priority to JP1016181A priority Critical patent/JPS57126449A/en
Publication of JPS57126449A publication Critical patent/JPS57126449A/en
Publication of JPH0132812B2 publication Critical patent/JPH0132812B2/ja
Granted legal-status Critical Current

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  • Organic Low-Molecular-Weight Compounds And Preparation Thereof (AREA)
  • Agricultural Chemicals And Associated Chemicals (AREA)

Description

【発明の詳細な説明】[Detailed description of the invention]

本発明はジカルボン酸、アルカリ金属水酸化
物、および無機銅塩からジカルボン酸銅を複分解
反応により製造し、生成したジカルボン酸銅沈澱
を過、傾瀉などにより分離するに際し、 一般式 (但しRは水素又はメチル基を示す。) で示される単量体の重合体あるいは前記一般式の
単量体とアクリルアミドの共重合体を分離助剤と
して用いるジカルボン酸銅の製造方法にかかわ
り、その目的とするところは、分離助剤を用いる
ことにより、微細なジカルボン酸銅沈澱をフロツ
ク状とすることにより、過速度あるいは沈降速
度を増大させ、製造効率を向上させることにあ
る。 ジカルボン酸銅、たとえば、テレフタル酸、フ
マル酸などの銅塩は殺菌力の強い銅イオンをジカ
ルボン酸塩という安定な状態で保持しており、そ
の殺菌作用が長期間にわたつて持続されるので、
高い保護殺菌作用を有しており、農業用殺菌剤と
して極めて有用である。また塗料に配合して塗膜
に発生するカビや、その他の微生物による汚染、
破損を防ぐことができる。 従来から知られている製造方法、例えば米国特
許第3623896号に記載の方法あるいは、Ind.Eng.
Chem.Prod.Res.Develop.、Vol.9、No.3、1970、
pg.408に記載の方法では、まずジカルボン酸銅を
苛性ソーダのようなアルカリ金属水酸化物の水溶
液に完全に溶解させて、ジカルボン酸アルカリ金
属塩水溶液をつくり、一方、硫酸銅五水塩のよう
な水溶性無機銅塩を水にとかして水溶液とし、こ
のどちらか一方に他方を加えて混合することによ
り、ジカルボン酸銅を得ている。しかし、複分解
反応の結果生成するジカルボン酸銅の沈澱は、極
めて微細なものであり、真空過機、加圧過機
のような通常工業的に用いられる過技術あるい
は、遠心分離機のような分離技術を用いても、沈
澱生成後短時間で、沈澱を水から分離することは
事実上不可能である。従つて従来法では、テレフ
タル酸銅の沈澱が生成後、そのまま8時間から12
時間放置して、ジカルボン酸銅水和物の結晶を成
長させ、吸引過等の技術によつて、容易に沈澱
を水から分離できる大きさに結晶粒が成長するの
を待つて、分離を行つている。このような従来か
らの方法では、ジカルボン酸銅の沈澱が生成して
から、次の操作である過などによる沈澱の分離
操作に移るまでに長時間を要し、操作の連続性が
損われ、この点が製造効率上の問題点となつてい
た。本発明は、ジカルボン酸アルカリ金属塩水溶
液と水溶性無機銅塩水溶液とかつ複分解反応によ
り、ジカルボン酸銅の沈澱を生成させ、この沈澱
を生成後直ちに停滞なく反応液より過等の技術
により分離する方法として、一般式()で表わ
される単量体の単独重合体あるいは、これとアク
リルアミドの共重合体の水溶液を沈澱生成後の反
応液に加え、ジカルボン酸銅の沈澱をフロツク状
となし、沈澱生成後直ちに、過あるいは、傾瀉
等の分離技術により、極めて容易にかつ短時間に
沈澱を反応液水層より分離するものである。 ジカルボン酸銅のような陽の表面電荷をもつと
考えられる重金属塩の沈澱の凝集あるいは、過
促進には、一般式()で表わされる単量体の重
合体のようなカチオン性凝集剤は元来不適とされ
てきている。しかしながら本発明者は、一般式
()で表わされる単量体の重合体、例えば、ジ
メチルアミノエチルメタクリレートの四級化塩等
の重合体は、ジカルボン酸銅の沈澱のフロツク形
成に少量で極めて有効であることを見い出し本発
明を完成した。さらにジカルボン酸銅は農業用殺
菌剤等として多くの病害にすぐれた効果を示す
が、本発明の分離助剤、即ち一般式()で表わ
されるビニル単量体の単独重合体あるいは、これ
とアクリルアミドの共重合体はこれら分離助剤自
身の特開昭54−32624号によればタバコ、キユウ
リ、トマトのモザイクビールスに対し、優れた防
除効果を示すことが記載されており、農業用殺菌
剤として用いられるジカルボン酸銅の製造に用い
られる補助薬剤としては本発明の分離助剤は好適
なものである。 ジカルボン酸アルカリ金属塩水溶液および無機
銅塩水溶液より複分解反応によりジカルボン酸銅
を製造する方法に於ては、ジカルボン酸銅の沈澱
を反応液水層より分離したのち、沈澱の水洗、再
スラリー化、スプレードライヤーによる乾燥、マ
イクロナイザーによる微粉砕の工程を経るのが普
通であるが、用いられた分離助剤がこれらの工程
中で何らかの障害となつてはならない。本発明に
於て用いられる分離助剤、例えば、ジメチルアミ
ノエチルメタクリレートの四級化塩等の重合体
は、ジカルボン酸銅沈澱分離後の工程に対しても
何ら障害を与えず、例えば、乾燥後小型マイクロ
ナイザーで微粉砕したテレフタル酸銅粉末の粒径
は分離助剤で用いない製法で得た製品が1.90ミク
ロンであつたのに対し、本発明で用いられる分離
助剤であるジメチルアミノエチルメタリレートの
四級化塩の重合体を用いた製品は1.35ミクロンで
あつた。またジカルボン酸銅は農業用殺菌剤とし
て多くの病害の予防にすぐれた効果を示すが、ジ
カルボン酸銅を水和剤として使用する場合には、
製品の水に対する分散性が、薬効、薬害にも影響
してくる。上に述べたマイクロナイザーで微粉砕
したテレフタル酸銅粉末に分散剤として、リグニ
ンスルホン酸ソーダ(商品名サンエツキス)を加
えたものについて、水に対する分散性を試験した
ところ、ジメチルアミノエチルメタクリレート四
級化塩等の重合体を用いて得た製品の分散性は用
いない製品の分散性よりすぐれていた。さらにこ
のテレフタル酸銅製品を実際に農業用殺菌剤とし
て、実地に使用し、キユウリの黒星病の防除試験
を行つた。その結果、ジメチルアミノエチルメタ
クリレート四級塩の重合体等を分離助剤として用
いて得た製品は、用いないで得た製品と同等以上
の効果を示した。本発明で用いられる分離助剤、
例えば、ジメチルアミノエチルメタクリレート四
級化塩等の単独重合体、あるいはこの単量体とア
クリルアミドの共重合体は、通常のラジカル重合
で得られる製品で、凝集沈澱剤として入手できる
ものである。これら分離助剤の本発明に於ける使
用量は、1バツチ当り得られるジカルボン酸銅の
収量の計算値に対して、0.1から5.0重量%でよ
い。分離助剤は0.1から5.0重量%程度の水溶液と
して、ジカルボン酸銅沈澱生成後の反応液に加
え、撹拌することにより、沈澱のフロツクを形成
させる。 本発明で用いられる分離助剤としては、具体的
には、ジメチルアミノエチル(メタ)アクリレー
トの重合体又はそれらとアクリルアミドの共重合
体のメチルクロライド四級塩等が挙げられる。ジ
カルボン酸とは、テレフタル酸、イソフタル酸、
フタル酸、フマル酸、マレイン酸、マジピン酸、
グルタミン酸、アスパラギン酸等をさし、無機銅
塩としては、硫酸銅、硫酸第二銅、塩化第二銅等
やこれらの水和塩等をさし、アルカリ金属とは、
苛性ソーダ、苛性カリ等をさす。次に本発明の実
施例を示す。 実施例 1 純度93%の苛性ソーダ43g(1モル)を水に溶
解し、全容を1リツトルとし、これにテレフタル
酸83g(0.5モル)を溶解させる。別に純度99%
の硫酸銅五水塩252g(1モル)を水に溶解し、
全容を1リツトルとする。この硫酸銅水溶液50ml
を撹拌しつつ、テレフタル酸ナトリウム水溶液
100mlを加え、テレフタル酸銅の沈澱を生成させ
る。5分間撹拌を続けたのち、表1に記載の凝集
沈澱剤Aの0.1重量%水溶液50mlを添加し、5分
間撹拌した。 この懸濁液を直径7.6cmのブツフナー斗に東
洋紙No.2(直径7cm)をしいたものの上に移し、
アスピレーターで5分間吸引した。5分後に吸引
過をやめ、吸引ビン中の液をメスシリンダー
に移し、液量を読みとつた。 表1の他の凝集沈澱剤についても同様の試験を
行つた。結果を表1に示す。
In the present invention, copper dicarboxylate is produced from dicarboxylic acid, alkali metal hydroxide, and inorganic copper salt by double decomposition reaction, and when the produced copper dicarboxylate precipitate is separated by filtration, decantation, etc., the general formula (However, R represents hydrogen or a methyl group.) Concerning a method for producing copper dicarboxylate using a polymer of a monomer represented by the formula or a copolymer of a monomer of the above general formula and acrylamide as a separation aid, The purpose of this is to use a separation aid to turn fine dicarboxylic acid copper precipitates into flocs, thereby increasing the overspeed or sedimentation rate and improving production efficiency. Copper dicarboxylate, such as copper salts such as terephthalic acid and fumaric acid, retain copper ions with strong bactericidal power in a stable state as a dicarboxylate, and their bactericidal action is sustained over a long period of time.
It has a high protective fungicidal effect and is extremely useful as an agricultural fungicide. In addition, contamination by mold and other microorganisms that occur on the paint film when mixed with paint,
Damage can be prevented. Conventionally known manufacturing methods, such as the method described in US Pat. No. 3,623,896 or Ind.Eng.
Chem.Prod.Res.Develop., Vol.9, No.3, 1970,
In the method described on pg.408, copper dicarboxylate is first completely dissolved in an aqueous solution of alkali metal hydroxide such as caustic soda to create an aqueous solution of alkali metal dicarboxylate; A copper dicarboxylate is obtained by dissolving a water-soluble inorganic copper salt in water to form an aqueous solution, and adding and mixing one of the two with the other. However, the precipitate of copper dicarboxylate produced as a result of the double decomposition reaction is extremely fine, and it cannot be removed using conventional industrial filtration techniques such as a vacuum filtration machine or pressure filtration machine, or separation techniques such as a centrifugal separator. Even using technology, it is virtually impossible to separate the precipitate from the water within a short time after its formation. Therefore, in the conventional method, after the copper terephthalate precipitate is formed, it is left as is for 8 to 12 hours.
The crystals of the copper dicarboxylate hydrate are allowed to grow for a period of time, and separation is carried out by waiting for the crystal grains to grow to a size that allows the precipitate to be easily separated from the water using techniques such as suction filtration. It's on. In such conventional methods, it takes a long time from the time the copper dicarboxylate precipitate is formed to the next step, which is separation of the precipitate by filtration, which impairs the continuity of the operation. This point has been a problem in terms of manufacturing efficiency. The present invention involves producing a precipitate of copper dicarboxylate through a double decomposition reaction between an aqueous solution of an alkali metal salt of a dicarboxylate and an aqueous solution of a water-soluble inorganic copper salt, and immediately separating this precipitate from a reaction solution without stagnation by an advanced technique. As a method, an aqueous solution of a homopolymer of the monomer represented by the general formula () or a copolymer of this and acrylamide is added to the reaction solution after precipitation, and the precipitate of copper dicarboxylate is made into a floc-like form. Immediately after formation, the precipitate can be separated from the aqueous layer of the reaction solution very easily and in a short time by separation techniques such as filtration or decanting. Cationic flocculants such as polymers of monomers represented by the general formula ( It has been considered inappropriate since then. However, the present inventor has discovered that a polymer of the monomer represented by the general formula (), such as a quaternized salt of dimethylaminoethyl methacrylate, is extremely effective in small amounts in forming a floc of copper dicarboxylate precipitate. We have discovered that this is the case and have completed the present invention. Furthermore, copper dicarboxylate exhibits excellent effects against many diseases as an agricultural fungicide, etc., but the separation aid of the present invention, that is, a homopolymer of vinyl monomers represented by the general formula (), or a combination of this and acrylamide According to Japanese Patent Application Laid-Open No. 54-32624, which describes the separation aid itself, the copolymer is described to have an excellent control effect against mosaic viruses of tobacco, cucumber, and tomato, and is used as an agricultural fungicide. The separation aid of the present invention is suitable as an auxiliary agent used in the production of copper dicarboxylate. In the method for producing copper dicarboxylate by metathesis reaction from an aqueous solution of an alkali metal dicarboxylate and an aqueous inorganic copper salt, the precipitate of copper dicarboxylate is separated from the aqueous layer of the reaction solution, and then the precipitate is washed with water, reslurried, It is common to go through the steps of drying with a spray dryer and pulverizing with a micronizer, but the separation aid used must not cause any hindrance during these steps. The separation aid used in the present invention, for example, a polymer such as a quaternized salt of dimethylaminoethyl methacrylate, does not pose any hindrance to the process after copper dicarboxylic acid precipitation and separation. The particle size of the copper terephthalate powder finely pulverized with a small micronizer was 1.90 microns for the product obtained by a manufacturing method that does not use a separation aid, whereas the particle size of the copper terephthalate powder, which is a separation aid used in the present invention, was 1.90 microns. The product using the polymer of the quaternized salt of the rate was 1.35 microns. Copper dicarboxylate is also highly effective as an agricultural fungicide in preventing many diseases, but when copper dicarboxylate is used as a hydrating agent,
The dispersibility of a product in water also affects its medicinal efficacy and drug damage. When we tested the dispersibility in water of copper terephthalate powder finely pulverized using the micronizer mentioned above and adding sodium ligninsulfonate (trade name: Sun-Etsukiss) as a dispersant, we found that dimethylaminoethyl methacrylate quaternized The dispersibility of products obtained using polymers such as salts was superior to that of products obtained without the use of polymers. Furthermore, this copper terephthalate product was actually used as an agricultural fungicide, and a test was conducted to control scab disease on cucumbers. As a result, a product obtained using a polymer of dimethylaminoethyl methacrylate quaternary salt as a separation aid showed an effect equal to or better than a product obtained without using it. Separation aid used in the present invention,
For example, a homopolymer such as dimethylaminoethyl methacrylate quaternized salt or a copolymer of this monomer and acrylamide is a product obtained by ordinary radical polymerization and can be obtained as a flocculating precipitant. The amount of these separation aids used in the present invention may be from 0.1 to 5.0% by weight based on the calculated yield of copper dicarboxylate obtained per batch. The separation aid is added as an aqueous solution of about 0.1 to 5.0% by weight to the reaction solution after the copper dicarboxylate precipitate is formed, and is stirred to form a precipitate floc. Specific examples of the separation aid used in the present invention include methyl chloride quaternary salts of polymers of dimethylaminoethyl (meth)acrylate or copolymers of these and acrylamide. Dicarboxylic acids include terephthalic acid, isophthalic acid,
Phthalic acid, fumaric acid, maleic acid, marzipic acid,
It refers to glutamic acid, aspartic acid, etc.; inorganic copper salts include copper sulfate, cupric sulfate, cupric chloride, etc., and their hydrated salts; alkali metals include:
Refers to caustic soda, caustic potash, etc. Next, examples of the present invention will be shown. Example 1 43 g (1 mol) of caustic soda with a purity of 93% is dissolved in water to make a total volume of 1 liter, and 83 g (0.5 mol) of terephthalic acid is dissolved in this. Except for 99% purity
Dissolve 252g (1 mol) of copper sulfate pentahydrate in water,
The total volume is 1 liter. 50ml of this copper sulfate aqueous solution
While stirring, add sodium terephthalate aqueous solution.
Add 100 ml to form a precipitate of copper terephthalate. After continuing to stir for 5 minutes, 50 ml of a 0.1% by weight aqueous solution of coagulation precipitant A listed in Table 1 was added and stirred for 5 minutes. Transfer this suspension onto a 7.6 cm diameter Buthunerto plate covered with Toyo Paper No. 2 (7 cm diameter).
Suction was performed using an aspirator for 5 minutes. After 5 minutes, suction was stopped, the liquid in the suction bottle was transferred to a graduated cylinder, and the amount of liquid was read. Similar tests were conducted on other flocculating precipitants shown in Table 1. The results are shown in Table 1.

【表】【table】

【表】 実施例 2 実施例1で調製したテレフタル酸ナトリウム水
溶液100mlをとつて撹拌し、同じく実施例1で調
製した硫酸銅水溶液50mlをこれに加え、テレフタ
ル酸銅の沈澱を生成させる。5分間撹拌を続けた
のち表2に記載の凝集沈澱剤Aの0.1重量%水溶
液60mlを添加し、5分間撹拌する。 こののち、この懸濁液を1リツトルのメスシリ
ンダーに移し、水を加えて全容を1リツトルと
し、ガラス棒で懸濁液を良く撹拌したのち静置し
た。5分後にメスシリンダーの底に沈んだ沈澱の
容積をメスシリンダーの目盛から読みとつた。 表2の他の凝集沈澱剤についても同様の試験を
行つた。 結果を表2に示す。
[Table] Example 2 100 ml of the sodium terephthalate aqueous solution prepared in Example 1 was taken and stirred, and 50 ml of the copper sulfate aqueous solution also prepared in Example 1 was added thereto to form a precipitate of copper terephthalate. After continuing stirring for 5 minutes, 60 ml of a 0.1% by weight aqueous solution of coagulation precipitant A listed in Table 2 was added and stirred for 5 minutes. Thereafter, this suspension was transferred to a 1 liter measuring cylinder, water was added to bring the total volume to 1 liter, the suspension was well stirred with a glass rod, and then left to stand. After 5 minutes, the volume of the precipitate that had settled to the bottom of the graduated cylinder was read from the scale of the graduated cylinder. Similar tests were conducted on other flocculating precipitants shown in Table 2. The results are shown in Table 2.

【表】【table】

【表】 * 商品名は表1に同じ
** 30分後の沈降沈澱容積
実施例1及び実施例2で用いた本発明の分離助
剤の組成を示す。 凝集沈澱剤A 凝集沈澱剤B 上記Aと同じ 凝集沈澱剤C 試験例 実施例1の凝集沈澱剤Aを用いて製造したテレ
フタル酸銅を水洗後、乾燥し、乳鉢で租粉砕し
た。このテレフタル酸銅をさらに、ザ・ジエツ
ト・パルバライザー社製のマイクロナイザー「ミ
クロン・マスター」02−505型を用いて微粉砕し、
フイツシヤー・サイエンテイフイツク社製のフイ
ツシヤー・サブーシーブ・サイザーを用いて粒径
を測定した。凝集沈澱剤Aを用いて製造したテレ
フタル酸銅の平均粒径は1.35ミクロンであり、凝
集沈澱剤を用いないで製造したテレフタル酸銅の
平均粒径は1.90ミクロンであつた。この微粉砕し
たテレフタル酸銅を用いて、キユウリの黒星病の
防除試験を行つた。鉢植えのキユウリ(トキワの
地這)に銅濃度として360ppmおよび540ppmにな
るように、調製したテレフタル酸銅の水性懸濁液
をガラス噴霧器を用いて散布し、風乾させた。翌
日、黒星病菌種をスプレー接種し、フアイロンハ
ウス内で17−23℃多湿度の条件下で、接触後5日
間放置し、病斑を形成させた。 一区四連制のポツト試験で、病斑形成の葉数を
調べ、病斑形成阻止率を求めたところ、わずかに
凝集沈澱剤Aを用いたものが、無添加のものより
も優つていた。
[Table] *Product names are the same as in Table 1 **Sedimentation volume after 30 minutes The composition of the separation aid of the present invention used in Examples 1 and 2 is shown. Coagulation precipitant A Coagulating precipitant B Same as above A Coagulating precipitating agent C Test Example Copper terephthalate produced using the coagulation precipitant A of Example 1 was washed with water, dried, and crushed in a mortar. This copper terephthalate was further finely ground using a micronizer "Micron Master" model 02-505 manufactured by The Jet Pulverizer Co., Ltd.
Particle size was measured using a Fisher Subsieve Sizer manufactured by Fisher Scientific. The average particle size of copper terephthalate produced using coagulation precipitating agent A was 1.35 microns, and the average particle size of copper terephthalate produced without using coagulating precipitant A was 1.90 microns. Using this finely pulverized copper terephthalate, a control test for scab disease of cucumbers was conducted. Aqueous suspensions of copper terephthalate prepared at copper concentrations of 360 ppm and 540 ppm were sprayed onto potted cucumbers using a glass sprayer, and air-dried. The next day, the seeds were spray-inoculated with scoliosis fungi and left in a heat iron house under humid conditions of 17-23°C for 5 days after contact to form lesions. In a pot test of four consecutive plots, the number of leaves with lesion formation was examined and the rate of inhibition of lesion formation was determined. Ta.

Claims (1)

【特許請求の範囲】 1 ジカルボン酸、アルカリ金属水酸化物および
無機銅塩よりジカルボン酸銅を複分解反応により
製造し、次いで、生成したジカルボン酸銅の沈澱
を水層より分離するに際し、 一般式 (但しRは水素又はメチル基を示す。) で示される単量体の重合体あるいは前記一般式の
単量体とアクリルアミドの共重合体を分離助剤と
して用いることを特徴とするジカルボン酸銅の製
造方法。
[Claims] 1. When copper dicarboxylate is produced from a dicarboxylic acid, an alkali metal hydroxide, and an inorganic copper salt by a metathesis reaction, and then the precipitate of the copper dicarboxylate produced is separated from the aqueous layer, the general formula (However, R represents hydrogen or a methyl group.) Copper dicarboxylate, characterized in that a polymer of the monomer represented by the formula or a copolymer of the monomer of the above general formula and acrylamide is used as a separation aid. Production method.
JP1016181A 1981-01-28 1981-01-28 Preparation of copper dicarboxylate Granted JPS57126449A (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
JP1016181A JPS57126449A (en) 1981-01-28 1981-01-28 Preparation of copper dicarboxylate

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
JP1016181A JPS57126449A (en) 1981-01-28 1981-01-28 Preparation of copper dicarboxylate

Publications (2)

Publication Number Publication Date
JPS57126449A JPS57126449A (en) 1982-08-06
JPH0132812B2 true JPH0132812B2 (en) 1989-07-10

Family

ID=11742552

Family Applications (1)

Application Number Title Priority Date Filing Date
JP1016181A Granted JPS57126449A (en) 1981-01-28 1981-01-28 Preparation of copper dicarboxylate

Country Status (1)

Country Link
JP (1) JPS57126449A (en)

Also Published As

Publication number Publication date
JPS57126449A (en) 1982-08-06

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