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JPS6028533B2 - Manufacturing method of heavy metal adsorbent - Google Patents
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JPS6028533B2 - Manufacturing method of heavy metal adsorbent - Google Patents

Manufacturing method of heavy metal adsorbent

Info

Publication number
JPS6028533B2
JPS6028533B2 JP51099299A JP9929976A JPS6028533B2 JP S6028533 B2 JPS6028533 B2 JP S6028533B2 JP 51099299 A JP51099299 A JP 51099299A JP 9929976 A JP9929976 A JP 9929976A JP S6028533 B2 JPS6028533 B2 JP S6028533B2
Authority
JP
Japan
Prior art keywords
uranium
adsorbent
group
copolymer
acid
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
JP51099299A
Other languages
Japanese (ja)
Other versions
JPS5323891A (en
Inventor
博 中山
裕子 谷口
久司 谷
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.)
Kanebo Ltd
Original Assignee
Kanebo 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 Kanebo Ltd filed Critical Kanebo Ltd
Priority to JP51099299A priority Critical patent/JPS6028533B2/en
Publication of JPS5323891A publication Critical patent/JPS5323891A/en
Publication of JPS6028533B2 publication Critical patent/JPS6028533B2/en
Expired legal-status Critical Current

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Classifications

    • YGENERAL 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
    • Y02TECHNOLOGIES OR APPLICATIONS FOR MITIGATION OR ADAPTATION AGAINST CLIMATE CHANGE
    • Y02PCLIMATE CHANGE MITIGATION TECHNOLOGIES IN THE PRODUCTION OR PROCESSING OF GOODS
    • Y02P10/00Technologies related to metal processing
    • Y02P10/20Recycling

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  • Solid-Sorbent Or Filter-Aiding Compositions (AREA)
  • Manufacture And Refinement Of Metals (AREA)
  • Inorganic Compounds Of Heavy Metals (AREA)

Description

【発明の詳細な説明】 本発明は水中に溶存するウランに対して選択的吸着能を
有する重金属吸着剤の製造方法に関する。
DETAILED DESCRIPTION OF THE INVENTION The present invention relates to a method for producing a heavy metal adsorbent having selective adsorption ability for uranium dissolved in water.

従来金属イオン吸着剤としてはカチオン又はアニオン交
モ剣樹脂やポリアミン系、ィミノ酢酸系のキレート樹脂
等が知られている。
Conventional metal ion adsorbents include cationic or anionic resins, polyamine-based chelate resins, and iminoacetic acid-based chelate resins.

これ等の樹脂は多種類の金属を無差別に吸着して、特定
の有用金属に対する選択吸着性に乏しく、例えば海水中
に溶存するウランを吸着採取する場合、吸着能を全く有
しない。
These resins adsorb many types of metals indiscriminately and have poor selective adsorption ability for specific useful metals. For example, when collecting uranium dissolved in seawater by adsorption, they have no adsorption ability at all.

近時、該ウランに対して吸着能を有するものとしてチタ
ン酸、レゾルシンヒ酸樹脂、トリアミノフェノールグリ
オキザール樹脂等が提案されているが吸着能は小さく又
水中での形状保持が不安定である等の理由により実用化
されていない。
Recently, titanic acid, resorcinol arsenic acid resin, triaminophenol glyoxal resin, etc. have been proposed as having adsorption ability for uranium, but their adsorption ability is small and their shape retention in water is unstable. It has not been put into practical use for some reason.

本発明者等は上記せる問題点を鱗消すべく鋭意広範囲に
系統的研究を行ない本発明を完成したものであり、その
目的とするところは水中に溶存する重金属特にウランに
対して優れた選択性と高吸着能を有する重金属吸着剤の
製造方法を提供するにある。即ち本発明はポリアミノス
チレン系共重合体をジアゾ化した後、一般式(1)(但
しR,〜R4は水素、アセチル基、ニトロ基、力ルボキ
シル基、水酸基、メチル基、メトキシ基を表わし、その
うち少なくとも1つは水素である。
The inventors of the present invention have completed the present invention by diligently and extensively conducting systematic research to eliminate the above-mentioned problems. and a method for producing a heavy metal adsorbent having high adsorption capacity. That is, in the present invention, after diazotizing a polyaminostyrene copolymer, the general formula (1) (where R, to R4 represent hydrogen, an acetyl group, a nitro group, a hydroboxyl group, a hydroxyl group, a methyl group, a methoxy group, At least one of them is hydrogen.

)で表わされるカテコール誘導体とカップリング反応せ
しめることを特徴とする重金属吸着剤の製造方法である
。本発明に用いるポリアミノスチレン系共重合体とはポ
リスチレン系共重合体例えばスチレンージビニルベンゼ
ン共重体、スチレンービニルピリジン共重合体、スチレ
ンークロルメチルスチレン共重合体をァミン類により架
橋せしめたもの等をニトロ化して還元することにより得
られる。
) is a method for producing a heavy metal adsorbent, which is characterized by carrying out a coupling reaction with a catechol derivative represented by: The polyaminostyrene copolymer used in the present invention is a polystyrene copolymer such as styrene-divinylbenzene copolymer, styrene-vinylpyridine copolymer, styrene-chloromethylstyrene copolymer crosslinked with amines, etc. It is obtained by nitrating and reducing.

ポリスチレン系共重合体のニトロ化は常法により濃硝酸
−濃硫酸混合系で50〜10000の温度下でニトロ化
することが望ましい。
It is preferable to nitrate the polystyrene copolymer using a conventional method using a mixed system of concentrated nitric acid and concentrated sulfuric acid at a temperature of 50 to 10,000 ℃.

温度が5000より低いと、反応速度が遅くなり、長時
間を要し、又10000より高いと、基体が損傷したり
、酸化を受けやすくなる。
If the temperature is lower than 5,000, the reaction rate will be slow and it will take a long time, and if it is higher than 10,000, the substrate will be damaged or susceptible to oxidation.

更に該ニトロ基をアミノ基に還元するに際しては、例え
ば、エタノール中で、ニトロ化ポリスチレン系共重合体
を濃塩酸と塩化第一錫と共に加熱還流する方法により達
成出来る。ニトロ化の際のポリスチレン系共重合体の架
橋度が低い場合、ポリマーが融解、又は豚着を生じるた
め長時間を要して反応させる必要が生ずる。
Further, the reduction of the nitro group to an amino group can be achieved, for example, by heating and refluxing the nitrated polystyrene copolymer together with concentrated hydrochloric acid and stannous chloride in ethanol. If the degree of cross-linking of the polystyrene copolymer during nitration is low, the polymer may melt or become clogged, making it necessary to carry out the reaction over a long period of time.

この場合、ニトロ化率は低下する傾向がある。又、架橋
度が高過ぎる場合、ニトロ化率が低下する傾向を示し、
これが最終的に、カテコール誘導体との反応率にも影響
を与える為適宜条件を選択することが好ましく、例えば
スチレンとジビニルベンゼンとを乳化重合、又は懸濁重
合により共重合するに際し、ジビニルベンゼンの仕込み
比率をスチレンに対し、0.5〜30モル%、特に好ま
しくは、0.5〜5モル%とすることにより、ニトロ化
の際上記難点を克服することが出来る。この場合のニト
ロ化率は、全ベンゼン核の80〜95%である。又、ス
チレンとクロルメチルスチレンを共重合せしめるに際し
クロルメチルスチレンの仕込み比率がスチレンに対して
5〜100モル%が好ましく得られた共重合体を織末と
するか、又は繊維状にしてアミン類例えばエチレンジア
ミン、ジェチレントリアミン、トリエチレンテトラミン
、ピベラジン、キシリレンジアミンの如く少なくとも二
官能性を有するアミンと水又はメタノール、ェタノール
、プロパノール、プタノールの如きアルコール類、或は
アセトン、メチルエチルケトンの如きケトン類、更には
アセトニトリル、ニトロメタン、ジメチルホルムアモド
、ジメチルアセトアミド、ジメチルスルホキシド等の溶
媒中で室温から50〜90qoの温度に1〜1加時間で
徐々に昇温して処理し架橋せしめる。
In this case, the nitration rate tends to decrease. In addition, if the degree of crosslinking is too high, the nitration rate tends to decrease,
Since this ultimately affects the reaction rate with the catechol derivative, it is preferable to select conditions appropriately. For example, when copolymerizing styrene and divinylbenzene by emulsion polymerization or suspension polymerization, the preparation of divinylbenzene By setting the ratio to styrene in a range of 0.5 to 30 mol%, particularly preferably 0.5 to 5 mol%, the above-mentioned difficulties during nitration can be overcome. The nitration rate in this case is 80 to 95% of all benzene nuclei. In addition, when copolymerizing styrene and chloromethylstyrene, the copolymer obtained preferably has a charging ratio of chloromethylstyrene of 5 to 100% by mole relative to styrene, and is used as a woven powder or in the form of fibers to form amines. For example, an amine having at least bifunctionality such as ethylenediamine, jethylenetriamine, triethylenetetramine, piperazine, and xylylenediamine, and water or alcohols such as methanol, ethanol, propanol, and butanol, or ketones such as acetone and methyl ethyl ketone, Further, it is treated in a solvent such as acetonitrile, nitromethane, dimethylformamod, dimethylacetamide, dimethylsulfoxide, etc. by gradually increasing the temperature from room temperature to 50 to 90 qo over 1 to 1 heating time to effect crosslinking.

この場合、昇温速度が上記条件より大きい場合、粉末、
或いは繊維状物質の表面が融解し、互いに豚着してガム
状となる。
In this case, if the temperature increase rate is higher than the above conditions, the powder,
Alternatively, the surfaces of the fibrous materials melt and stick to each other, forming a gum-like state.

この方法により得られる粉末状或いは繊維状物質は、不
熔不融性が高く、ニトロ化の条件にも耐ることが出来、
又ニトロ化率は全ベンゼン核の75〜95%である。上
記方法により得られるポリアミノスチレン系共重合体は
次にジアゾ化する。この際談共重合体の形状は粉末状或
は繊維状が好ましい。ポリアミノスチレン系共重合体を
該共重合体のアミノ基量に対して3倍モル量の塩酸を含
有する水溶液に浸潰し0〜10午0の温度下で燭拝しな
がら亜硝酸ソーダ水溶液を滴下する。
The powder or fibrous material obtained by this method has high inmeltability and infusibility and can withstand nitration conditions.
Further, the nitration rate is 75 to 95% of all benzene nuclei. The polyaminostyrene copolymer obtained by the above method is then diazotized. The shape of this copolymer is preferably powder or fiber. A polyaminostyrene copolymer is soaked in an aqueous solution containing 3 times the molar amount of hydrochloric acid based on the amount of amino groups in the copolymer, and a sodium nitrite aqueous solution is added dropwise at a temperature of 0 to 10 o'clock. do.

この際、亜硝酸ソーダの飽和量は沃素デンプン試験紙を
用いて知ることが出来る。
At this time, the saturated amount of sodium nitrite can be determined using iodine starch test paper.

即ち、沃素デンプン紙が青色を示し、且、数分以上退色
しない点を以つて、飽和量とする。これに似つて、該ポ
リアミノスチレン系共重合体のジアゾ化を受けるァミノ
基の量が解る。
That is, the saturation amount is defined as the point at which the iodine starch paper exhibits a blue color and does not fade for more than a few minutes. Similarly, the amount of amino groups that undergo diazotization in the polyaminostyrene copolymer can be determined.

ジアゾ化を完了した該共重合体は、炉別し徐々に、カテ
コール系誘導体をアミ/基量の1〜1折音モル溶解した
10%苛性ソーダ水溶液に加え、一5〜10午○で窒素
雰囲気中、1〜2岬時間蝿拝してカップリングを完了す
る。本発明に使用する前記一般式で示されるカテコール
譲導体としては、例えば、カテコール3−ニトロカテコ
ール、4ーニトロカテコール、5ーニトロピロガノール
、2,3−ジオキシ安息香酸、3,4ージオキシ安息香
酸、2,3,4ートリオキシ安息香酸、3−メチルカテ
コール、4−メチルカテコール、3−メトキシカテコー
ル、4ーメトキシカテコール、2,3ージオキシアセト
フエニン、3,4−ジオキシアセトフエノン、2,3,
4−トリオキシアセトフエノン、2,3−ジオキシ−4
ーメトキシーアセトフェノン等が拳げられる。
The diazotized copolymer was separated from the furnace and gradually added to a 10% aqueous solution of caustic soda in which a catechol derivative was dissolved in an amount of 1 to 1 molar of the amino/base amount, and the mixture was heated in a nitrogen atmosphere at 15 to 10 o'clock. In the middle, fly worship for 1-2 hours to complete the coupling. Examples of the catechol derivatives represented by the above general formula used in the present invention include catechol 3-nitrocatechol, 4-nitrocatechol, 5-nitropyroganol, 2,3-dioxybenzoic acid, and 3,4-dioxybenzoic acid. Acid, 2,3,4-trioxybenzoic acid, 3-methylcatechol, 4-methylcatechol, 3-methoxycatechol, 4-methoxycatechol, 2,3-dioxyacetophenone, 3,4-dioxyacetophenone ,2,3,
4-trioxyacetophenone, 2,3-dioxy-4
- Methoxyacetophenone etc. are exposed.

特に前記一般式で示されるカテコール誘導体のうちで分
子中にニトロ基、アセチル基、カルボキシル基を有する
ものをジアゾカップリングした吸着剤は吸着能がより優
れており、又R,にこれ等の基を有するものの場合、更
に優れた吸着能を示した。
Particularly, among the catechol derivatives represented by the above general formula, adsorbents obtained by diazo coupling of those having nitro groups, acetyl groups, and carboxyl groups in the molecule have better adsorption ability. In the case of the one having , even better adsorption ability was shown.

本発明の吸着剤の製造過程に於ける反応の確認及び分析
は次の方法により行なった。
Confirmation and analysis of reactions in the manufacturing process of the adsorbent of the present invention were performed by the following method.

即ちポリスチレン系共重合体のニトロ化反応に於いて、
反応率はケルダール窒素分析法により窒素を測定し、こ
れからニトロ基の量を決定した。
That is, in the nitration reaction of polystyrene copolymers,
The reaction rate was determined by measuring nitrogen by Kjeldahl nitrogen analysis method, and the amount of nitro groups was determined from this.

又ニトロ化された共重合体の赤外吸収スペクトルは、1
520肌‐1,1340cの‐1に、ニトロ基に由釆す
る吸収を有する。又、ジアゾ化の際の亜硝酸ソーダの飽
和量からジアゾ化を受けるアミノ基を測定した。
In addition, the infrared absorption spectrum of the nitrated copolymer is 1
520 skin-1,1340c-1 has absorption due to nitro group. In addition, the amino groups undergoing diazotization were measured from the saturated amount of sodium nitrite during diazotization.

これによりニトロ基の95〜100%がアミノ基還元さ
れていることを確認した。更に前記ジアゾ化共重合体と
カテコール誘導体とのカップリング反応率は、反応前後
のカテコール誘導体水溶液の吸光度を測定して決めるこ
とが出来る。
This confirmed that 95 to 100% of the nitro groups were reduced to amino groups. Further, the coupling reaction rate between the diazotized copolymer and the catechol derivative can be determined by measuring the absorbance of the aqueous catechol derivative solution before and after the reaction.

吸光度の測定は350〜23肌mの間で行い、極大吸収
を用いた方が正確である。
It is more accurate to measure absorbance between 350 and 23 skin meters and use maximum absorption.

これから決められた反応率は、ジアゾ化を受けたアミノ
基量の25〜50%であった。本発明方法により得られ
る吸着剤をケルダール法により窒素分析を行ない、この
値より推定したカップリング反応率は吸光度測定より求
めた反応率の10%誤差の範囲にあった。
The reaction rate determined from this was 25-50% of the amount of diazotized amino groups. The adsorbent obtained by the method of the present invention was subjected to nitrogen analysis using the Kjeldahl method, and the coupling reaction rate estimated from this value was within a 10% error of the reaction rate determined from absorbance measurement.

本発明方法により得られる吸着剤を用いて、ウランを吸
着させるに際しては、該吸着剤をカラムに充填し又は繊
維状、薄膜状等の形状でウラン含有水として接触せしめ
るか、或いは該吸着剤をウラン含有水に浸糟し、縄拝す
る。
When adsorbing uranium using the adsorbent obtained by the method of the present invention, the adsorbent is packed in a column or brought into contact with uranium-containing water in the form of fibers, thin films, etc., or the adsorbent is Immerse yourself in uranium-containing water and worship on a rope.

ウラン含有水のpH値は4〜9.5の間で、ウラン吸着
能は良好であり、特に好ましくは5.5〜9である。
The pH value of the uranium-containing water is between 4 and 9.5, and the uranium adsorption ability is good, and the pH value is particularly preferably between 5.5 and 9.

pH値が4以下、或いは9.5以上ではウラン吸着量は
低下する。本発明による吸着剤は海水等のウラン濃度が
低く、多種類の重金属が共存する水溶液からでもウラン
を効率よく吸着補集することが出来、その選択性は極め
て高いものである。
When the pH value is below 4 or above 9.5, the amount of uranium adsorbed decreases. The adsorbent according to the present invention is capable of efficiently adsorbing and collecting uranium even from an aqueous solution in which the uranium concentration is low, such as seawater, and many types of heavy metals coexist, and its selectivity is extremely high.

吸着されたウランは、硫酸、塩酸、硝酸等の酸金属によ
っては炭酸ソーダ、炭酸アンモニウム、苛性ソーダ、ア
ンモニア等のアルカリを含有する水溶液により吸着剤か
ら容易に脱離、回収することが出来るものでありその工
業的利用価値は極めて大きいものである。
Adsorbed uranium can be easily desorbed and recovered from the adsorbent with an aqueous solution containing an alkali such as soda carbonate, ammonium carbonate, caustic soda, or ammonia, depending on the acid metal such as sulfuric acid, hydrochloric acid, or nitric acid. Its industrial utility value is extremely large.

以下実施例について説明する。Examples will be described below.

実施例 1 1モル%のジピニルベンゼンを含有するスチレン10の
こ界面活性剤2夕(花王ァトラス社製:商品名ェマール
10を1夕、共栄社油脂製商品名:ノニオライトPN−
12を1夕)を加えて240ccの水に乳化させ、窒素
気流中過硫酸カリ0.1夕を加えて80午○で激しく澄
拝する。
Example 1 Styrene 10 surfactant containing 1 mol% dipinylbenzene (manufactured by Kao Atlas Co., Ltd., trade name: EMAL 10), Kyoeisha Yushi Co., Ltd., trade name: Noniolite PN-
12) was added for 1 night to emulsify it in 240 cc of water, 0.1 night of potassium persulfate was added in a nitrogen stream, and the mixture was vigorously purified at 80 pm.

30分後、1モル%のジビニルベンゼンを含むスチレン
70夕を1時間要して滴下し、更に、この系を濃塩酸を
加えて破壊し、ポリスチレン系共重合体を炉別洗浄する
After 30 minutes, 70 g of styrene containing 1 mol % of divinylbenzene was added dropwise over a period of 1 hour, and the system was further destroyed by adding concentrated hydrochloric acid, and the polystyrene copolymer was washed in a furnace.

このポリスチレン粉末を乾燥し、7夕を濃硝酸15cc
、濃硫酸40cc中に70午0で澱拝しながら、2時間
掛けて加え、更に70午0で30分、反応させた後、砕
氷中に注ぐ。
Dry this polystyrene powder and add 15 cc of concentrated nitric acid to
The mixture was added to 40 cc of concentrated sulfuric acid over 2 hours while being stirred at 70:00, and after reacting for another 30 minutes at 70:00, it was poured into crushed ice.

この様にして得たニトロ化ポリスチレンは十分乾燥した
後、乾燥した。得られた共重合中の全窒素量をケルダー
ル法により測定したところ、100雌サンプル中、0.
68hMの窒素を含有していた。
The nitrated polystyrene thus obtained was thoroughly dried and then dried. When the total amount of nitrogen in the resulting copolymerization was measured by the Kjeldahl method, it was found that out of 100 female samples, 0.
It contained 68 hM nitrogen.

これからニトロ化率を計算すると、全ベンゼン核の94
%がニトロ化を受けていることになる。続いてこの重合
体をエタノール80cc、濃塩酸70cc中で塩化第一
錫2水塩60夕と共に1脚寿間加熱還流した後、炉過し
、水洗、が苛性ソーダ水溶液で洗浄後水洗して次にジア
ゾ化を行なう。
Calculating the nitration rate from this, 94 of the total benzene nuclei
% has undergone nitration. Subsequently, this polymer was heated under reflux in 80 cc of ethanol and 70 cc of concentrated hydrochloric acid with stannous chloride dihydrate for 60 min, filtered in an oven, washed with water, washed with an aqueous solution of caustic soda, and then washed with water. Perform diazotization.

該アミノ化ポリスチレン1夕を水25cc、IN−塩酸
25ccに懸濁し氷冷し5℃以下に保った燈、激しく蝿
拝しながら、亜硝酸ソーダの1モル溶液を徐々に滴下し
7.8ccでヨウ素デンプン試験紙は明瞭な青紫色を呈
した。
One night of the aminated polystyrene was suspended in 25 cc of water and 25 cc of IN-hydrochloric acid, cooled on ice, and kept below 5°C. While shaking vigorously, a 1 molar solution of sodium nitrite was gradually added dropwise to 7.8 cc. The iodine starch test paper exhibited a clear blue-purple color.

従って、この値から全ニトロ基の殆んど全てが還元され
、又アミノ基の97〜99%がジアゾ化を受けたと考え
られる。ジアゾ化を行なった重合体は素遠く炉別し、氷
水で洗浄する。
Therefore, from this value, it is considered that almost all of the nitro groups were reduced and 97 to 99% of the amino groups were diazotized. The diazotized polymer is separated from the furnace and washed with ice water.

3−ニトロカテコール3.1夕を、10%苛性ソーダ5
0ccに溶解し、窒素雰囲気中で0〜3℃保った状態で
、該ジアゾ化重合体を少量ずつ加えた後0℃で24時間
燈拝し、カップリング反応を行なった。
3-nitrocatechol 3.1% and 10% caustic soda 5%
The diazotized polymer was dissolved in 0 cc and maintained at 0 to 3° C. in a nitrogen atmosphere, and the diazotized polymer was added little by little, followed by heating at 0° C. for 24 hours to perform a coupling reaction.

反応終了後樹脂は炉別し、水洗した後、風乾して吸着剤
を得た。カップリング反応率は反応前後の溶液中の3−
ニトロカテコールの吸光度測定から求めた。
After the reaction was completed, the resin was separated in a furnace, washed with water, and air-dried to obtain an adsorbent. The coupling reaction rate is 3- in the solution before and after the reaction.
It was determined by measuring the absorbance of nitrocatechol.

反応液lccをサンプリングし、2%苛性ソーダで2.
5そとする。この吸光度を島津製作所製UV−200を
用いて29加mに於いて測定した。これから計算すると
3.1mMの3ーニトロカテコールが反応したことにな
る。従ってジアゾ化を受けたアミノ基の約40%がカッ
プリング反応を行ったと考えられる。この様にして得ら
れた吸着剤に就いて、ウラン吸着テストを行なった。
The reaction solution lcc was sampled and diluted with 2% caustic soda.
5. This absorbance was measured at 29 m using UV-200 manufactured by Shimadzu Corporation. Calculating from this, it means that 3.1mM of 3-nitrocatechol reacted. Therefore, it is considered that about 40% of the diazotized amino groups underwent the coupling reaction. A uranium adsorption test was conducted on the adsorbent thus obtained.

ウラン500ムタを硝酸ウラニルとして添加した天然海
水5〆中に該吸着剤100の9を入れ、30qoで2岬
時間鷹梓後吸着剤を炉別し乾燥した試料を理学電気製ガ
イガーフレックスSX蟹光X線分析装置によりウランを
定量した。その結果吸着剤100雌当り385ムタのウ
ランを吸着していた。これは吸着剤1夕当りに換算して
3.85の9を吸着したことになり、又全ウランの77
%を回収したことになる。比較例として既知吸着剤であ
るチタン酸、レゾルシンーヒ酸樹脂、2,4,6−トリ
アミノフェノールグリオキザール樹脂の各々100の9
を吸着剤として前記方法と同様に吸着テストを行なった
結果をあわせて第1表に示す。
9 parts of the adsorbent was placed in natural seawater to which 500 parts of uranium had been added as uranyl nitrate, and the adsorbent was heated for 2 hours at 30 qo, then the adsorbent was separated in a furnace and the dried sample was placed in a Geigerflex SX crab light manufactured by Rigaku Denki. Uranium was determined using an X-ray analyzer. As a result, 385 muta of uranium was adsorbed per 100 pieces of adsorbent. This means that 9 of 3.85 uranium was adsorbed per night of adsorbent, and 77 of total uranium was adsorbed.
% has been recovered. As comparative examples, titanic acid, resorcinol-arsenic acid resin, and 2,4,6-triaminophenol glyoxal resin, which are known adsorbents, were each used at 9/100.
Table 1 shows the results of an adsorption test conducted in the same manner as in the above method using the adsorbent as the adsorbent.

但しチタン酸は、四塩化チタン塩酸溶液を苛性ソーダで
中和して得られたものである。
However, titanic acid is obtained by neutralizing titanium tetrachloride hydrochloric acid solution with caustic soda.

又、レゾルシンーヒ酸樹脂はしゾルシンーヒ酸を通常の
方法でホルマリン重合して得られるものである。又、2
,4,6−トリアミノフェノールーグリオキザール樹脂
は2,4,6−トリアミノフヱノ−ルとグリオキザール
を酸触媒で縮合重合して得られたものである。第1表 次に蜜光X線測定を行なった吸着剤をとり出し、IN塩
酸10ccに70℃で浸潰し、更に再度同機の処理を行
って、ウランを溶出させ、液中のウランをフッ化ナトリ
ウム球法により紫外蟹光を測定した結果溶出液中ウラン
は380〃夕であった。
Further, resorcinol-arsenic acid resin is obtained by formalin polymerization of resorcinol-arsenic acid in a conventional manner. Also, 2
, 4,6-triaminophenol-glyoxal resin is obtained by condensation polymerization of 2,4,6-triaminophenol and glyoxal using an acid catalyst. Table 1 Next, the adsorbent that was subjected to the honeycomb X-ray measurement was taken out and immersed in 10 cc of IN hydrochloric acid at 70°C, and the same treatment was performed again to elute the uranium and fluoride the uranium in the liquid. As a result of measuring ultraviolet light using the sodium sphere method, the amount of uranium in the eluate was 380.

従つて、この3−ニトロカテコールーアゾースチレン樹
脂に吸着されたウランは容易にほぼ完全に脱着される。
以上の様に上記本発明により得られる吸着剤は優れたウ
ラン吸着能力をもち、その吸着速度選択性の点でも非常
に良好であることが繁る。
Therefore, the uranium adsorbed on the 3-nitrocatechol-azostyrene resin is easily and almost completely desorbed.
As described above, the adsorbent obtained according to the present invention has excellent uranium adsorption ability, and often has very good adsorption rate selectivity.

実施例 2 スチレンージビニルベンゼン共重合体をジビニルベンゼ
ンのスチレンに対する仕込み比率を0〜40モル%の間
で変えて、乳化重合せしめて英重合体を得た。
Example 2 A styrene-divinylbenzene copolymer was subjected to emulsion polymerization while changing the charging ratio of divinylbenzene to styrene between 0 and 40 mol % to obtain a polymer.

乳化重合は実施例1と同様に行い、得られた共重合体の
ニトロ化、還元、ジアゾカップリングに就いても、実施
例1と同じ方法で行い、吸着剤を得た。ジアゾカップリ
ングを行うに際して、カテコール譲導体として5ーニト
ロピロガノールを用い、アミノポリスチレン系共重合体
1夕に対し、5−ニトロピロガロール3.4夕を反応さ
せ、反応率は28別伽吸光度で測定した。得られた吸着
剤のウラン吸着テスト、ウラン吸着量の分析は実施例1
と同様に行なった。
Emulsion polymerization was performed in the same manner as in Example 1, and nitration, reduction, and diazo coupling of the obtained copolymer were performed in the same manner as in Example 1 to obtain an adsorbent. When performing diazo coupling, 5-nitropyroganol was used as a catechol derivative, and 3.4 days of 5-nitropyrogallol was reacted with 1 day of aminopolystyrene copolymer, and the reaction rate was 28% absorbance. It was measured with The uranium adsorption test of the obtained adsorbent and the analysis of the amount of uranium adsorbed were performed in Example 1.
I did the same thing.

結果を第2表に示す。第2表第2表の結果から鱗る様に
、ジアゾ化当量はジビニルベンゼンの共重合比率が30
モル%を超えると、著しく低下し実用に通さなくなる。
The results are shown in Table 2. Table 2 As can be seen from the results in Table 2, the diazotization equivalent is determined when the copolymerization ratio of divinylbenzene is 30.
If it exceeds mol%, it will drop significantly and become impractical.

又ジビニルベンゼンを含有しないポリスチレンはニトロ
化条件を緩和せざるを得ない為、ポリマー中の官能基量
は減少したと考えられる。実施例 3 スチレン85部に対し、クロルメチルスチレン25部を
混合し、窒素置換した封管中で、過酸化ペンゾィルを開
始剤とし、80午0で塊重合を行なう。
Moreover, since the nitration conditions for polystyrene not containing divinylbenzene had to be relaxed, it is thought that the amount of functional groups in the polymer was reduced. Example 3 85 parts of styrene and 25 parts of chloromethylstyrene were mixed, and bulk polymerization was carried out at 8:00 AM using penzoyl peroxide as an initiator in a sealed tube purged with nitrogen.

得られたポリマーを180午0で溶融紡糸し、径10一
の繊維とする。これをジェチレントリアミンの20%エ
タノール溶媒中に浸潰し、3ぴ○で3時間蝿拝した後、
3時間掛けて70qo迄徐々に昇温し、その後更に70
00で2時間、処理する。この様にして得られた繊維を
、実施例1と同様に、ニトロ化、還元ジアゾカップリン
グ反応を行なった。
The obtained polymer is melt-spun at 180 mm to obtain fibers with a diameter of 10 mm. This was immersed in a 20% ethanol solvent of jethylene triamine, and after being heated for 3 hours at 3 pi○,
The temperature was gradually raised to 70 qo over 3 hours, and then further increased to 70 qo.
00 for 2 hours. The fiber thus obtained was subjected to nitration and reduction diazo coupling reaction in the same manner as in Example 1.

ジアゾカップリングを行なうに際してカナコール誘導体
として2,3,4ートリオキシアセトフェノンを用い、
繊維1のこ対し、5夕の2,3,4−トリオキシアセト
フェノンを反応させ、反応率を27別mの吸光度より求
めた。各反応率は、ニトロ化が全ベンゼン核の約90%
であり、ジアゾ化を受けたアミノ基は7.1mM/夕、
2,3,4ートリオキシアセトフェノンの反応量は3.
1mMであった。この繊維状吸着剤300のoを径1伽
のカラムに5肌長さに充填し重炭酸ソーダでpH8.5
とした硝酸ウラニル水溶液(ウラン濃度5ムタ/そ)5
0〆を4虫時間掛けて通液した。
When performing diazo coupling, 2,3,4-trioxyacetophenone is used as a canacol derivative,
The fiber 1 was reacted with 2,3,4-trioxyacetophenone for 5 days, and the reaction rate was determined from the absorbance at 27 meters. The rate of each reaction is approximately 90% of the total benzene nuclei nitrated.
and the diazotized amino group was 7.1mM/night,
The reaction amount of 2,3,4-trioxyacetophenone is 3.
It was 1mM. 300 ml of this fibrous adsorbent was packed into a column with a diameter of 1 C to 5 skin lengths, and the pH was adjusted to 8.5 with sodium bicarbonate.
Aqueous uranyl nitrate solution (uranium concentration 5 mta/so) 5
The solution was passed through the tube for 4 hours.

吸着ウランを0.州−塩酸100ccで脱着し、液中ウ
ラン量をフッ化ナトリウム球法により蟹光光度計で測定
した。その結果、脱着ウランは235ムタであり、繊維
状吸着剤は、ほぼ完全にウランを吸着していた。従って
、この吸着剤は、低濃度のウランを吸着する場合に於い
ても優れた効果を示すものである。実施例 4 実施例1として得たアミノ化ポリスチレンと、ジアゾカ
ップリングする際本発明のカテコール誘導体と、その他
のフェノール系化合物を反応させ実施例1と同じ方法で
吸着テストを行なった。
Adsorbed uranium to 0. It was desorbed with 100 cc of hydrochloric acid, and the amount of uranium in the liquid was measured using a crab photometer using the sodium fluoride ball method. As a result, the amount of uranium desorbed was 235 Muta, and the fibrous adsorbent had almost completely adsorbed uranium. Therefore, this adsorbent exhibits excellent effects even when adsorbing low concentrations of uranium. Example 4 An adsorption test was conducted in the same manner as in Example 1 by reacting the aminated polystyrene obtained in Example 1 with the catechol derivative of the present invention and other phenolic compounds during diazo coupling.

結果を第3表に示す。第3表 上記化合物をジアゾカップリングした際の反応率、即ち
、ポリマーのアミノ基のうち、ジアゾカップリングを受
けたアミノ基の百分率は32〜40%の間にあり、バラ
ツキがあるが、本発明のカテコール議導体と、他の例に
拳げたフェノール系化合物では吸着量に大きな差のある
ことが鮫る。
The results are shown in Table 3. Table 3: The reaction rate when the above compound was diazo-coupled, that is, the percentage of amino groups that underwent diazo coupling among the amino groups of the polymer was between 32 and 40%, and although there was some variation, this It can be seen that there is a large difference in adsorption amount between the catechol conductor of the invention and other phenolic compounds.

実施例 5実施例3で用いたポIJアミノスチレン系繊
維に本発明のカテコール誘導体をジアゾカップリングし
、吸着テストを行なった。
Example 5 The catechol derivative of the present invention was diazo-coupled to the poly-IJ aminostyrene fiber used in Example 3, and an adsorption test was conducted.

反応方法は実施例1に従い吸着テストは、吸着剤100
mgを天然海水50そ中で、5日間縄拝した。第4表に
、吸着結果と、吸光度より求めた反応率を示す。反応率
はジアゾ化を受けたアミノ基のうちカップリングしたも
のの百分率である。第4表 第4表に拳げた様に、吸着量はニトロ基、アセチル基、
カルボキシル基を有する吸着剤が優れており2,3−ジ
オキシ−4ーメトキシアセトフヱノン>3,4ージオキ
シアセトフエノン、2,3ージオキシ安息香酸>3,4
ージオキシ安息香酸、4ーニトロピロガロール>3ーニ
トロカナコール>4−ニトロカテコール、の如く、カテ
コールの水酸性に隣接した位置に、これ等の基がある場
合ウラン吸着量が大きくなる効果が認められる。
The reaction method was carried out in accordance with Example 1, and the adsorption test was carried out using adsorbent 100
50mg was roped in natural seawater for 5 days. Table 4 shows the adsorption results and the reaction rate determined from the absorbance. The reaction rate is the percentage of diazotized amino groups that are coupled. Table 4 As shown in Table 4, the adsorption amount is nitro group, acetyl group,
Adsorbents with carboxyl groups are excellent; 2,3-dioxy-4-methoxyacetophenone>3,4-dioxyacetophenone, 2,3-dioxybenzoic acid>3,4
-dioxybenzoic acid, 4-nitropyrogallol > 3-nitrocanacol > 4-nitrocatechol, when these groups are located adjacent to the hydroxyl property of catechol, the effect of increasing the amount of uranium adsorption is observed. .

天然海水中にはウランが3.3仏夕/そ程溶存して居り
、良いものでは約70%回収したことになる。
There is approximately 3.3 ml of uranium dissolved in natural seawater, and approximately 70% of the good material has been recovered.

実施例 6 実施例5の2,3−ジオキシ安息香酸をカップリング固
定した繊維500の9をウラン水溶液(ウランにして2
の9/そとなる様に硝酸ウラニルを用いて調整した。
Example 6 9 of 500 fibers in which 2,3-dioxybenzoic acid of Example 5 was coupled and fixed were mixed with a uranium aqueous solution (2
It was adjusted using uranyl nitrate to make it 9/so.

pH‘ま6.5である。)2のこ浸潰し、5時間燈拝し
てウランを吸着させ、蟹光X線法によりウランを定量し
た。ウラン吸着量は吸着剤100の夕当り、720メタ
であった。該吸着剤100の9を次の様な方法で処理し
、ウランを溶出させた。‘1ー 0.州‐塩酸25cc
中60qoで30分浸燈しこれを2回繰り返す。
pH' is 6.5. ) 2. The mixture was soaked and crushed, and uranium was adsorbed by lighting for 5 hours, and uranium was quantified using the crab light X-ray method. The amount of uranium adsorbed was 720 meth per evening on the adsorbent 100. Nine of the 100 adsorbents were treated in the following manner to elute uranium. '1-0. State - Hydrochloric acid 25cc
Soak for 30 minutes at medium 60qo and repeat this twice.

■ 0.1N−硫酸25cc中に、20qoで1時間浸
潰し、これを2回繰り返す。
(2) Soak in 25 cc of 0.1N sulfuric acid at 20 qo for 1 hour, and repeat this twice.

【31 10%炭酸アンモニウム水溶液50cc中で6
0oo、3び分処理する。
[31 6 in 50 cc of 10% ammonium carbonate aqueous solution
0oo, process 3 times.

【4)5%の炭酸ソーダと、5%の重炭酸ソーダを含む
水溶液50ccに30o○、1時間浸債する。
[4] Soak in 50 cc of an aqueous solution containing 5% soda carbonate and 5% bicarbonate at 30°C for 1 hour.

以上の方法で脱着させたウランをフッ化ナトリウム球法
により実施例1と同様に測定した。熔出ウラン量と、脱
着率を第5表に示す。第5表 第5表から解る様に脱着方法は如何なる方法であっても
ほぼ完全に脱着出来る。
The uranium desorbed by the above method was measured in the same manner as in Example 1 using the sodium fluoride sphere method. Table 5 shows the amount of uranium dissolved and the desorption rate. Table 5 As can be seen from Table 5, any method of attachment and detachment allows for almost complete attachment and detachment.

実施例 7 実施例1と同様にして得たポリアミノスチレン系共重合
体と2,3ージオキシ安息香酸(1),2,3,4ート
リオキシアセトフエノン(0)をジアゾカップリングし
、吸着剤(1)(ロ)を得た。
Example 7 A polyaminostyrene copolymer obtained in the same manner as in Example 1 and 2,3-dioxybenzoic acid (1), 2,3,4-trioxyacetophenone (0) were diazo-coupled and adsorbed. Agent (1) (b) was obtained.

この二つの吸着剤につき、塩化亜鉛、硝酸鉛、硝酸第二
鉄、塩化スチロンチウム、塩化第二銅、硝酸ニッケル、
硝酸ウラニルを各々3仏M溶かした水溶液100〆を重
炭酸ソーダでpH7.5とし、吸着剤100の9を入れ
2独時間、室温で燈拝し、吸着した金属を蟹光X線分析
した。
For these two adsorbents, zinc chloride, lead nitrate, ferric nitrate, styrontium chloride, cupric chloride, nickel nitrate,
A 100ml aqueous solution containing 3ml each of uranyl nitrate was adjusted to pH 7.5 with sodium bicarbonate, 100ml of adsorbent was added, and the mixture was allowed to stand at room temperature for 2 hours, and the adsorbed metals were subjected to crab-light X-ray analysis.

その結果を第6表に示す。The results are shown in Table 6.

第6表 第6表から解る様に本発明方法による吸着剤は特にウラ
ンに対して高い選択性をもつことが解る。
Table 6 As can be seen from Table 6, the adsorbent produced by the method of the present invention has particularly high selectivity for uranium.

Claims (1)

【特許請求の範囲】 1 ポリアミノスチレン系共重合体をジアゾ化した後
一般式(1) ▲数式、化学式、表等があります▼ (但しR_1〜R_4は水素、アセチル基、ニトロ基、
カルボキシル基、水酸基、メチル基又はメトキシ基を表
わし、そのうち少なくとも1つは水素である。 )で表わされるカテコール誘導体とカツプリング反応せ
しめることを特徴とする重金属吸着剤の製造方法。2
一般式(1)に於いてR_1がニトロ基、アセチル基又
はカルボキシル基である特許請求の範囲第1項記載の重
金属吸着剤の製造方法。
[Claims] 1. After diazotizing the polyaminostyrene copolymer
General formula (1) ▲There are mathematical formulas, chemical formulas, tables, etc.▼ (However, R_1 to R_4 are hydrogen, acetyl group, nitro group,
It represents a carboxyl group, a hydroxyl group, a methyl group or a methoxy group, at least one of which is hydrogen. ) A method for producing a heavy metal adsorbent, which comprises carrying out a coupling reaction with a catechol derivative represented by: 2
The method for producing a heavy metal adsorbent according to claim 1, wherein R_1 in general formula (1) is a nitro group, an acetyl group, or a carboxyl group.
JP51099299A 1976-08-19 1976-08-19 Manufacturing method of heavy metal adsorbent Expired JPS6028533B2 (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
JP51099299A JPS6028533B2 (en) 1976-08-19 1976-08-19 Manufacturing method of heavy metal adsorbent

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
JP51099299A JPS6028533B2 (en) 1976-08-19 1976-08-19 Manufacturing method of heavy metal adsorbent

Publications (2)

Publication Number Publication Date
JPS5323891A JPS5323891A (en) 1978-03-04
JPS6028533B2 true JPS6028533B2 (en) 1985-07-05

Family

ID=14243746

Family Applications (1)

Application Number Title Priority Date Filing Date
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Country Status (1)

Country Link
JP (1) JPS6028533B2 (en)

Cited By (1)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
KR20200138177A (en) 2018-03-29 2020-12-09 쿠리타 고교 가부시키가이샤 Selective permeable membrane, its manufacturing method and water treatment method

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JP6193004B2 (en) * 2013-06-14 2017-09-06 株式会社日立ハイテクノロジーズ Adsorbent and analysis system using the same

Cited By (1)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
KR20200138177A (en) 2018-03-29 2020-12-09 쿠리타 고교 가부시키가이샤 Selective permeable membrane, its manufacturing method and water treatment method

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