JP2000140626A - Method for regenerating arsenic adsorbent - Google Patents

Method for regenerating arsenic adsorbent

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Publication number
JP2000140626A
JP2000140626A JP10322158A JP32215898A JP2000140626A JP 2000140626 A JP2000140626 A JP 2000140626A JP 10322158 A JP10322158 A JP 10322158A JP 32215898 A JP32215898 A JP 32215898A JP 2000140626 A JP2000140626 A JP 2000140626A
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JP
Japan
Prior art keywords
adsorbent
oxidizing agent
alkali
arsenic
treatment
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
JP10322158A
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Japanese (ja)
Other versions
JP3957899B2 (en
Inventor
Toshio Yotsumoto
利夫 四元
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SHIN NIPPON SALT KK
Original Assignee
SHIN NIPPON SALT KK
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Priority to JP32215898A priority Critical patent/JP3957899B2/en
Publication of JP2000140626A publication Critical patent/JP2000140626A/en
Application granted granted Critical
Publication of JP3957899B2 publication Critical patent/JP3957899B2/en
Anticipated expiration legal-status Critical
Expired - Lifetime legal-status Critical Current

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Abstract

PROBLEM TO BE SOLVED: To efficiently desorb arsenic adsorbed on an arsenic adsorbent to such a degree that the adsorbent can be reused by carrying out treatment with an alkali and an oxidizing agent. SOLUTION: A used arsenic adsorbent containing hydrous oxide of a rare earth element and/or hydrous oxide of zirconium is regenerated by treatment with an alkali and an oxidizing agent, preferably an oxidizing agent which does not deteriorate the structure and performance of the adsorbent. Hydrogen peroxide or sodium hypochlorite is particularly preferably used as the oxidizing agent. The oxidizing agent may be used alone before alkali treatment or may be used as a mixture with the alkali regenerating agent. When the oxidizing agent is used alone before alkali treatment, pH in reaction may be in any of acidic and alkaline regions. Hydroxide of an alkali metal may be used as the alkali agent and sodium hydroxide or potassium hydroxide is preferably used because a high desorption rate is attained.

Description

【発明の詳細な説明】DETAILED DESCRIPTION OF THE INVENTION

【0001】[0001]

【発明の属する技術分野】本発明は、砒素、特に亜ヒ酸
イオン吸着した吸着剤の再生方法に関するものである。
The present invention relates to a method for regenerating an adsorbent having arsenic ions, particularly arsenite ions, adsorbed thereon.

【0002】[0002]

【従来の技術】従来知られている砒素を吸着させた希土
類元素の水和酸化物、ジルコニアの水和酸化物を含有す
る吸着剤の再生方法は、高液比、高温の条件(たとえ
ば、特開昭61−187931号公報参照)で行うもの
で、再生が難しく、また脱着率も低いので、実質上、産
業廃棄物として処分しているのが現状である。
2. Description of the Related Art Conventionally known methods for regenerating an adsorbent containing a hydrated oxide of a rare earth element adsorbed with arsenic and a hydrated oxide of zirconia include conditions of high liquid ratio and high temperature (for example, (See Japanese Unexamined Patent Publication (Kokai) No. 61-187931), which is difficult to regenerate and has a low desorption rate, and is currently practically disposed of as industrial waste.

【0003】[0003]

【発明が解決しようとする課題】本発明は、砒素を吸着
した吸着剤を再生して再利用するために、脱着しやすい
条件を提供することを目的とするものである。
SUMMARY OF THE INVENTION An object of the present invention is to provide a condition for easy desorption in order to regenerate and reuse an adsorbent having adsorbed arsenic.

【0004】[0004]

【課題を解決するための手段】本発明者は、前記課題を
解決すべく鋭意研究を重ねた結果、本発明を完成するに
至った。すなわち、希土類元素の水和酸化物及び/又は
ジルコニアの水和酸化物を含有する砒素用吸着剤の再生
において、アルカリおよび酸化剤を用いて処理する吸着
剤再生方法である。本発明によれば、酸化剤は一般に亜
ヒ酸イオンをヒ酸イオンに酸化できるものであれば何で
もよく、吸着した砒素を効率的に脱着できる。
Means for Solving the Problems The inventors of the present invention have conducted intensive studies to solve the above-mentioned problems, and as a result, have completed the present invention. That is, in the regeneration of an arsenic adsorbent containing a hydrated oxide of a rare earth element and / or a hydrated oxide of zirconia, this is an adsorbent regeneration method in which treatment is performed using an alkali and an oxidizing agent. According to the present invention, the oxidizing agent may be any one which can oxidize arsenite ion into arsenite ion in general, and can efficiently desorb adsorbed arsenic.

【0005】本発明の希土類元素の水和酸化物とは、希
土類元素の酸化物および塩類の水酸化によって得られる
化合物で、単独または二種類以上の混合物もしくは各種
金属イオンを共存させて生成した複合金属水和酸化物で
ある。希土類元素はいずれを用いても良いが、セリウ
ム、ランタンを用いることができる。
[0005] The hydrated oxide of a rare earth element of the present invention is a compound obtained by hydroxylation of an oxide or a salt of a rare earth element, and may be used alone or as a mixture of two or more kinds or a complex formed by coexisting various metal ions. It is a metal hydrated oxide. Although any rare earth element may be used, cerium and lanthanum can be used.

【0006】使用する該酸化剤は吸着剤の構造や性能を
劣化させないものが好ましく、過酸化水素、次亜塩素酸
ソーダ等が特に好ましい。
The oxidizing agent used preferably does not degrade the structure and performance of the adsorbent, and hydrogen peroxide, sodium hypochlorite and the like are particularly preferable.

【0007】これらの酸化剤の使用方法は、アルカリ処
理前に単独で使用してもよいし、アルカリ再生剤に混合
して使用してもよい。アルカリ処理前に単独で使用する
場合反応pHは酸性、アルカリ性領域のどちらでも構わ
ない。該酸化剤の添加量は砒素吸着量に対して、モル比
で0.1倍量以上、好ましくは0.6倍量以上である。
[0007] These oxidizing agents may be used alone before the alkali treatment, or may be used as a mixture with an alkali regenerating agent. When used alone before the alkali treatment, the reaction pH may be in the acidic or alkaline range. The amount of the oxidizing agent to be added is at least 0.1 times, preferably at least 0.6 times the molar amount of the arsenic adsorption amount.

【0008】アルカリ剤としては、アルカリ金属の水酸
化物が使用でき、特に水酸化ナトリウムおよび水酸化カ
リウムは、脱着率が大きく特に好ましい。該アルカリ溶
液の濃度は吸着剤の種類によっても異なるが、0.1N
以上、好ましくは1N以上である。また、使用する該ア
ルカリ溶液の量は吸着剤の種類、接触方法等によって異
なり、浸漬によるバッチ再生では大量に使用しないと脱
着率は高くならない。しかし、処理液は大量の砒素を含
むため、凝沈等の処理が必要となることを考慮すると、
できるだけ少ない方が良く、吸着剤量に対して1〜20
倍量、好ましくは5〜12倍量が良い。
As the alkali agent, hydroxides of alkali metals can be used, and sodium hydroxide and potassium hydroxide are particularly preferable because of their high desorption ratio. The concentration of the alkaline solution varies depending on the type of the adsorbent.
Or more, preferably 1N or more. The amount of the alkaline solution used varies depending on the type of the adsorbent, the contact method, and the like. The batch regeneration by immersion does not increase the desorption rate unless a large amount is used. However, since the treatment liquid contains a large amount of arsenic, considering the necessity of treatment such as coagulation,
The smaller the better, the better the amount of adsorbent is 1-20
Double amount, preferably 5 to 12 times.

【0009】反応温度は、脱着速度および脱着平衡に影
響を与え、加温することは効果があるが、室温でも十分
効果を上げられる。また、接触時間は接触時の方法、温
度、吸着剤の種類によって左右されるが、通常、平衡に
達するのには1分〜3日程度であり、実用的には1分〜
180分でよい。
[0009] The reaction temperature affects the desorption rate and desorption equilibrium, and although heating is effective, the effect can be sufficiently increased even at room temperature. The contact time depends on the method, temperature and type of adsorbent at the time of contact, but it usually takes about 1 minute to 3 days to reach equilibrium, and practically 1 minute to
180 minutes is sufficient.

【0010】本発明の吸着剤は、希土類及びジルコニア
の水和酸化物およびこれを適当な多孔質担体に担持させ
る等の方法で粒状、糸状、帯状、板状等の任意の形状に
成形したものであればどんなものを用いてもよい。担体
に用いる材料は無機、有機の種々の材料が使用できるが
担持加工、担持強度、化学的耐久性等の面から、公知の
有機高分子材料が好ましい。また、無機多孔体中に析出
させたものでも構わない。
The adsorbent of the present invention is a hydrated oxide of rare earth and zirconia and formed into an arbitrary shape such as granular, thread-like, band-like or plate-like by a method of supporting the same on a suitable porous carrier. Anything may be used. As the material used for the carrier, various inorganic and organic materials can be used, but a known organic polymer material is preferable from the viewpoint of supporting processing, supporting strength, chemical durability and the like. Moreover, what precipitated in the inorganic porous body may be sufficient.

【0011】この吸着剤を例えば砒素を含有する水溶液
と接触させ、その水溶液中の砒素を吸着除去させた後、
この吸着剤を再生するのにこの発明が有効である。
The adsorbent is brought into contact with, for example, an aqueous solution containing arsenic, and the arsenic in the aqueous solution is adsorbed and removed.
The present invention is effective for regenerating the adsorbent.

【0012】[0012]

【発明の実施の形態】次に、実施例によって本発明をさ
らに詳細に説明する。
Now, the present invention will be described in further detail with reference to Examples.

【0013】実施例1〜5 本発明の再生操作において、酸化剤の種類および反応p
Hを変えた例を表1に示す。
Examples 1 to 5 In the regeneration operation of the present invention, the type of oxidizing agent and the reaction p
Table 1 shows examples in which H is changed.

【0014】砒素用吸着剤は次の方法で調製した。エチ
レン−ビニルアルコール共重合体(日本合成化学株式会
社製、ソアノールEタイプ)をジメチルスルフォキシド
に12重量%の濃度で溶解し、該溶液に含水酸化セリウ
ムを重合体量の6重量倍添加し、充分撹拌分散させた。
該混合物を凝固浴として水を用い、粒状に成形した。該
成形体を洗浄水に溶媒が検出されなくなるまで、水洗し
た。得られた吸着剤は平均粒径0.7mm、該水酸化セ
リウムの酸化セリウムとしての保持量0.4g/吸着剤
mlであった。
The arsenic adsorbent was prepared by the following method. An ethylene-vinyl alcohol copolymer (Soarnol E type, manufactured by Nippon Synthetic Chemical Co., Ltd.) is dissolved in dimethyl sulfoxide at a concentration of 12% by weight, and cerium hydroxide containing hydroxerium is added to the solution at 6 times the weight of the polymer. And sufficiently dispersed by stirring.
The mixture was formed into granules using water as a coagulation bath. The molded body was washed with water until no solvent was detected in the washing water. The obtained adsorbent had an average particle diameter of 0.7 mm, and the retention amount of the cerium hydroxide as cerium oxide was 0.4 g / ml of the adsorbent.

【0015】予め亜ヒ酸イオンを砒素として5mg−A
s/ml−吸着剤を吸着した上記吸着剤1mlを、砒素
吸着量に対して、モル比で2倍量になるように調整した
過酸化水素、次亜塩素酸ソーダ、ペルオキシ二硫酸ナト
リウムの3種の酸化剤水溶液100mlとビーカー中で
1時間混合、撹拌し、次にその溶液を廃棄し、アルカリ
再生液としてIN−NaOH溶液を用い、これに砒素用
吸着剤を浸漬、撹拌して20時間後の液中の砒素濃度を
測定して、脱着量を求めた。
5 mg-A of arsenic ion as arsenic
s / ml-3 ml of hydrogen peroxide, sodium hypochlorite, and sodium peroxydisulfate, in which 1 ml of the above adsorbent having adsorbed the adsorbent was adjusted so as to have a molar ratio twice as much as the arsenic adsorption amount. Mixing and stirring for 1 hour in a beaker with 100 ml of an aqueous solution of an oxidizing agent of the species, then discarding the solution, using an IN-NaOH solution as an alkali regenerating solution, immersing the adsorbent for arsenic in this and stirring for 20 hours The arsenic concentration in the liquid afterwards was measured to determine the amount of desorption.

【0016】この再生条件で、酸化剤処理時の液pHに
よらず、脱着率は35〜80%と高い値を示した。
Under these regeneration conditions, the desorption rate showed a high value of 35 to 80% regardless of the pH of the solution at the time of the oxidizing agent treatment.

【0017】[0017]

【表1】 [Table 1]

【0018】比較例1 実施例1〜5と同様の方法で、酸化剤を添加しない場合
の通常のアルカリ処理のみの結果を表1に示す。脱着率
が2%と極めて低いものであった。
Comparative Example 1 In the same manner as in Examples 1 to 5, Table 1 shows the results of ordinary alkali treatment alone when no oxidizing agent was added. The desorption rate was extremely low at 2%.

【0019】実施例6〜8 本発明の再生操作において、酸化剤の濃度を変えた例を
表2に示す。
Examples 6 to 8 Table 2 shows examples in which the concentration of the oxidizing agent was changed in the regeneration operation of the present invention.

【0020】実施例1〜5と同様の操作で調製した砒素
用吸着剤に、予め亜ヒ酸イオンを砒素として7mg−A
s/ml−吸着剤を吸着させたもの15mlを、内径2
4mm、長さ60mmのアクリル製カラムに充填した。
再生方法はアルカリ再生剤として、2N−NaOH溶液
180mlに酸化剤として次亜塩素酸ソーダを砒素に対
して、モル比で0.5、1.0、2.0倍量になるよう
に混合調整した水溶液を、SV4hr~1の速度で3時間
通水することで再生し、カラム出口液中の砒素濃度を測
定して脱着量を求めた。
The arsenic adsorbent prepared in the same manner as in Examples 1 to 5 was treated with 7 mg-A
s / ml-15 ml of adsorbent adsorbed, 2
A 4 mm, 60 mm long acrylic column was packed.
In the regeneration method, sodium hypochlorite as an oxidizing agent was mixed with 180 ml of a 2N-NaOH solution as an alkali regenerating agent to arsenic so that the molar ratio was 0.5, 1.0, and 2.0 times as much as arsenic. aqueous solution and regenerated by 3 hours through water at a rate of SV4hr ~ 1, was determined desorption amount by measuring the arsenic concentration in the column discharge solution.

【0021】この操作により、次亜塩素酸ソーダの添加
モル比0.5、1.0、2.0倍量において、脱着率は
高い値を示した。
By this operation, the desorption rate showed a high value when the molar ratio of sodium hypochlorite was 0.5, 1.0, and 2.0 times.

【0022】[0022]

【表2】 [Table 2]

【0023】比較例2 実施例6〜8と同様の方法で、酸化剤を添加しない場合
のアルカリ処理のみの結果を表2に示す。脱着率が2%
と極めて低いものであった。
Comparative Example 2 In the same manner as in Examples 6 to 8, Table 2 shows the results of only the alkali treatment when no oxidizing agent was added. 2% desorption rate
It was extremely low.

【0024】実施例9〜14 本発明の再生操作において、ジルコニアの水和酸化物か
らなる吸着剤を用い、アルカリ濃度と酸化剤添加の有無
による脱着率の関係について例を表3に示す。
Examples 9 to 14 In the regeneration operation of the present invention, Table 3 shows an example of the relationship between the alkali concentration and the desorption rate depending on whether or not an oxidizing agent is added, using an adsorbent composed of a hydrated oxide of zirconia.

【0025】砒素用吸着剤の作製方法は実施例1〜5と
同様の方法で、含水酸化セリウムの替わりに含水酸化ジ
ルコニウムを使用した。得られた吸着剤は平均粒径0.
8mm、該水酸化ジルコニウムの酸化物としての保持量
は0.17g/吸着剤mlであった。
The method for preparing the arsenic adsorbent was the same as in Examples 1 to 5, except that hydrous zirconium oxide was used instead of hydrous cerium hydroxide. The obtained adsorbent has an average particle size of 0.1.
8 mm, the retention amount of the zirconium hydroxide as an oxide was 0.17 g / ml of adsorbent.

【0026】予め亜ヒ酸イオンを砒素として4mg−A
s/ml−吸着剤を吸着した吸着剤3mlを、再生液と
して濃度0.2、2NのNaOHに、酸化剤(次亜塩素
酸ソーダ)添加量を砒素吸着量に対して、モル比で0.
34〜1.5倍量になるように混合調整した水溶液60
mlとビーカー中で混合、撹拌し、20時間後の液中の
砒素濃度を測定して、脱着量を求めた。
The arsenite ion was previously converted to arsenic by 4 mg-A
s / ml-3 ml of the adsorbent having adsorbed the adsorbent was used as a regenerating solution in 0.2% and 2N NaOH, and the amount of the oxidizing agent (sodium hypochlorite) added was 0 in molar ratio with respect to the amount of arsenic adsorbed. .
Aqueous solution 60 mixed and adjusted to 34-1.5 times volume
Then, the mixture was stirred in a beaker, and the arsenic concentration in the liquid after 20 hours was measured to determine the desorption amount.

【0027】この操作により、アルカリ濃度が低くて
も、酸化剤(次亜塩素酸ソーダ)を添加することによ
り、脱着率は56〜90%と高い値を示した。
By this operation, even when the alkali concentration was low, the desorption rate showed a high value of 56 to 90% by adding an oxidizing agent (sodium hypochlorite).

【0028】[0028]

【表3】 [Table 3]

【0029】比較例3〜6 実施例9〜14と同様の方法で、酸化剤を添加しない場
合のアルカリ処理のみの結果を表3に示す。酸化剤で処
理しない場合は、脱着率が8〜34%と低い値を示し
た。
Comparative Examples 3 to 6 In the same manner as in Examples 9 to 14, Table 3 shows the results of the alkali treatment alone when no oxidizing agent was added. When not treated with an oxidizing agent, the desorption rate showed a low value of 8 to 34%.

【0030】[0030]

【発明の効果】以上説明したように、本発明の再生方法
は、吸着した砒素を効率的に脱着させることができ、再
使用が可能な程度まで砒素が脱着できるので、砒素の処
理コストを大幅に削減することができる。
As described above, the regeneration method of the present invention can efficiently desorb adsorbed arsenic and can desorb arsenic to such an extent that it can be reused. Can be reduced.

Claims (1)

【特許請求の範囲】[Claims] 【請求項1】 希土類元素の水和酸化物及び/又はジル
コニアの水和酸化物を含有する砒素用吸着剤の再生にお
いて、アルカリおよび酸化剤を用いて処理することを特
徴とする吸着剤再生方法。
1. A method for regenerating an adsorbent for arsenic containing a hydrated oxide of a rare earth element and / or a hydrated oxide of zirconia, comprising treating with an alkali and an oxidizing agent. .
JP32215898A 1998-11-12 1998-11-12 Regeneration method of arsenic adsorbent Expired - Lifetime JP3957899B2 (en)

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* Cited by examiner, † Cited by third party
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Cited By (14)

* Cited by examiner, † Cited by third party
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JP2002205062A (en) * 2001-01-12 2002-07-23 Shin Nihon Salt Co Ltd Method for removing copper in salt water, method for regenerating copper adsorbing resin and apparatus for removing copper in salt water
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CN100381201C (en) * 2005-07-28 2008-04-16 刘转年 Composite adsorbent contg. flyash and its prepn. method
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JP2012143737A (en) * 2011-01-14 2012-08-02 National Institute For Materials Science Arsenic ion adsorbing element, method for detecting arsenic ion concentration in water using arsenic ion adsorbing element and method for removing arsenic from water
CN103338857A (en) * 2011-01-14 2013-10-02 独立行政法人物质材料研究机构 Nanostructure loaded with arsenic ion-adsorbing compound and arsenic ion recovery method using same
US9187343B2 (en) 2011-01-14 2015-11-17 National Institute For Materials Science Nanostructure material supporting arsenic ion adsorption compound and method to remove arsenic ion using the same
JP2013095641A (en) * 2011-11-01 2013-05-20 National Institute For Materials Science Mesoporous alumina loaded with arsenic ion-adsorbing compound, method for recovering arsenic ion using the same, and method for producing arsenic-free aqueous solution
ITVE20130025A1 (en) * 2013-05-09 2014-11-10 Gruppo Zilio S P A REGENERATION PROCEDURE OF FILTERING MATERIAL FOR ARSENIC.-
EP2801553A1 (en) * 2013-05-09 2014-11-12 Gruppo Zilio S.P.A. Process for the regeneration of iron oxyhydroxide-based filtration material for arsenic
CN103706321A (en) * 2013-09-26 2014-04-09 燕山大学 Zirconium oxide-brine shrimp egg shell biological composite absorption agent and preparation method

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