JPS6010521B2 - Chelate resin deodorization method - Google Patents
Chelate resin deodorization methodInfo
- Publication number
- JPS6010521B2 JPS6010521B2 JP3298077A JP3298077A JPS6010521B2 JP S6010521 B2 JPS6010521 B2 JP S6010521B2 JP 3298077 A JP3298077 A JP 3298077A JP 3298077 A JP3298077 A JP 3298077A JP S6010521 B2 JPS6010521 B2 JP S6010521B2
- Authority
- JP
- Japan
- Prior art keywords
- resin
- chelate
- chelate resin
- hot water
- impurities
- 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
Links
Landscapes
- Other Resins Obtained By Reactions Not Involving Carbon-To-Carbon Unsaturated Bonds (AREA)
- Addition Polymer Or Copolymer, Post-Treatments, Or Chemical Modifications (AREA)
Description
【発明の詳細な説明】
本発明はキレート樹脂製造工程において樹脂内部に残留
する溶媒および未反応モノマー等の不純物を樹脂内部か
ら除去するキレート樹脂の脱臭法に関するものである。DETAILED DESCRIPTION OF THE INVENTION The present invention relates to a method for deodorizing a chelate resin, which removes impurities such as solvents and unreacted monomers remaining inside the resin during the chelate resin manufacturing process.
キレート樹脂の製造に際し、製造過程で用いた溶媒およ
び禾反応モノマー等の不純物が生成キレート樹脂内部に
残留することは避けられない。かかる不純物を含有する
キレート樹脂は残留溶媒等に起因する臭を有するだけで
なく、これら不純物が重金属イオンの吸着の障害となる
ため商品化に際してこれらの不純物を除去する必要があ
る。そのため従来からキレート樹脂の製造過程でこれら
の不純物は除去されていたが、その除去方法は、たとえ
ばキレート樹脂を生成した後単なる送風による温風乾燥
法かあるいは真空下で加熱する減圧真空乾燥法または熱
水洗浄法等であった。しかるに、かかる温風乾燥法や減
圧真空加熱乾燥法は、キレート樹脂に熱をあたえて樹脂
内部の媒体およびモノマーが外部に出やすくすると同時
に樹脂外部の媒体やモノマーをすみやかに除去し、樹脂
外部濃度と樹脂内部濃度との差による媒体移動を行なっ
て除去するものであるから、不純物の除去速度は不純物
の樹脂内拡散速度が律遠となり脱臭処理に長時間を要し
た。When producing a chelate resin, it is inevitable that impurities such as the solvent and reactive monomer used in the production process remain inside the produced chelate resin. Chelate resins containing such impurities not only have an odor due to residual solvent, etc., but also these impurities impede the adsorption of heavy metal ions, so it is necessary to remove these impurities before commercialization. For this reason, these impurities have conventionally been removed during the manufacturing process of chelate resin, but methods for removing them include, for example, hot air drying by simply blowing air after producing chelate resin, reduced pressure vacuum drying by heating under vacuum, or Hot water washing method etc. However, such hot air drying methods and reduced pressure vacuum heating drying methods apply heat to the chelate resin to make it easier for the medium and monomers inside the resin to come out, while at the same time quickly removing the medium and monomers outside the resin, reducing the external concentration of the resin. Since the removal is carried out by moving the medium based on the difference between the concentration of the impurities and the internal concentration of the impurities, the rate of removal of impurities is determined by the rate of diffusion of the impurities within the resin, and the deodorizing process takes a long time.
一方熱水洗浄法は樹脂内拡散速度を上げるため、樹脂自
身を湿潤状態に保ち樹脂を膨?題させたのち、熱水と媒
体およびモノマーを入れ替えるため、前記の2方法と比
べ脱臭処理時間は短縮される。しかしこれら公知の脱臭
処理法はいずれもキレート樹脂を加熱状態に長時間さら
すものであるから、熱に対して比較的不安定なキレート
樹脂の官能基が破壊されキレート樹脂の性能は著しく低
下する。本発明者はかかる現状のキレート樹脂の脱臭法
の欠点を解決すべく鋭意研究した結果、キレート樹脂の
キレート官能基に重金属イオンを吸着させると官能基が
熱に対して著しく安定化し、しかも重金属イオンを吸着
した状態でもキレート樹脂内に残留する溶媒および未反
応モノマー等の不純物が熱り鷺こより容易に除去し得る
ことを見いだし本発明を完成した。On the other hand, the hot water cleaning method increases the diffusion rate within the resin by keeping the resin itself moist and allowing the resin to swell. After the deodorization, the hot water, medium, and monomer are replaced, so the deodorizing treatment time is shortened compared to the above two methods. However, since all of these known deodorizing treatment methods involve exposing the chelate resin to a heated state for a long period of time, the functional groups of the chelate resin, which are relatively unstable to heat, are destroyed and the performance of the chelate resin is significantly reduced. As a result of intensive research to solve the drawbacks of the current deodorizing methods for chelate resins, the present inventor found that when heavy metal ions are adsorbed to the chelate functional groups of chelate resins, the functional groups are significantly stabilized against heat, and the heavy metal ions The present invention was completed based on the discovery that impurities such as the solvent and unreacted monomers remaining in the chelate resin even when it is adsorbed can be easily removed by heating.
すなわち本発明はキレート樹脂に重金属イオンを交換吸
着させた後熱球に浸潰して該樹脂内部に残留する溶媒お
よびモノマー等の不純物を洗浄除去することを特徴とす
るキレート樹脂の脱臭法である。That is, the present invention is a deodorizing method for a chelate resin, which comprises exchanging and adsorbing heavy metal ions onto the chelate resin, and then immersing the resin in a hot bulb to wash and remove impurities such as solvents and monomers remaining inside the resin.
本発明の対象となるキレート樹脂としては、例えばスチ
レンジビニルベンゼソ共重合体、フェノール類−アルデ
ヒド類縮合体等の母体樹脂に官能基としてジェチレント
リアミソ、トリエチレンテトラミン、テトラエチレンベ
ンタミン、ベンタエチレンヘキサミン等のアミン類や、
ィミノニ酢酸あるいは上記アミン類とハロゲン化酢酸反
応物のアミノカルボン酸類ジェタノールアミン、ジブロ
パノールアミン等のアルコールアミン類、尿素、チオ尿
素等の尿素類を導入したものがあげられ、本発明の方法
はかかるキレート樹脂の製造工程で溶媒および未反応モ
ノマーが樹脂内部に残留する場合およびキレート樹脂の
使用時に溶媒が付着した場合の洗浄等に適用できる。Chelate resins to which the present invention is applied include, for example, styrene divinylbenzeso copolymer, phenol-aldehyde condensate, and other base resins with functional groups such as jethylenetriamiso, triethylenetetramine, tetraethylenebentamine, and bentamate. Amines such as ethylenehexamine,
Examples of the method of the present invention include aminocarboxylic acids obtained by reacting the above amines with halogenated acetic acid, alcohol amines such as jetanolamine and dibropanolamine, and ureas such as urea and thiourea. This can be applied to cleaning when solvents and unreacted monomers remain inside the resin during the manufacturing process of such chelate resins, and when solvents adhere to the chelate resins during use.
本発明の方法は製造過程に用いた溶媒および未反応モノ
マーを含有するキレート樹脂を、たとえば亜鉛、銅、ア
ルミニウム、ニッケル、カルシウム等の重金属イオンを
含有する水溶液で処理してキレート樹脂の官能基に重金
属イオンを吸着させ、次に重金属の吸着によりその官能
基を保護したキレート樹脂を好ましくは8000以上、
特に好ましくは9び0以上の熱水に浸潰してキレート樹
脂を洗浄するものである。The method of the present invention involves treating the chelate resin containing the solvent used in the manufacturing process and unreacted monomers with an aqueous solution containing heavy metal ions, such as zinc, copper, aluminum, nickel, and calcium, to convert the functional groups of the chelate resin into A chelate resin that adsorbs heavy metal ions and then protects its functional groups by adsorbing heavy metals, preferably 8000 or more,
Particularly preferably, the chelate resin is washed by immersion in hot water of 9 to 0 or more.
このときのキレート樹脂の洗浄方法としてはキレート樹
脂を熱水に浸潰して機械的に境拝する方法もあるが「熱
水に空気を送風するか加熱水蒸気を吹き込んで熱水を損
梓せしめる方法が樹脂の損傷等が起こらず好ましい。本
発明の方法で脱臭処理したキレート樹脂は通常の鉱酸水
溶液による脱離処理により容易に再生することができ、
この処理によってキレート樹脂の有するキレート形成能
も殆ど低下しない。しかし重金属イオンを吸着させない
で同様の熱水処理を行なうと、利用する熱水が高くなる
ほど脱臭処理後のキレート樹脂の性能は低下し、著しい
場合はキレート形成館の3割以上が破壊されることもあ
る。次に実施例により本発明をさらに詳細に説暁する。At this time, there is a method of cleaning the chelate resin by soaking the chelate resin in hot water and cleaning it mechanically, but there is also a method called "method of blowing air into the hot water or blowing heated steam to make the hot water deplete." is preferable because no damage to the resin occurs.The chelate resin deodorized by the method of the present invention can be easily regenerated by desorption treatment with a normal mineral acid aqueous solution.
This treatment hardly reduces the chelate forming ability of the chelate resin. However, if similar hot water treatment is performed without adsorbing heavy metal ions, the higher the hot water used, the lower the performance of the chelate resin after deodorizing treatment, and in severe cases, more than 30% of the chelate formation chamber may be destroyed. There is also. Next, the present invention will be explained in more detail with reference to Examples.
なお実施例中の部は重量部を表わす。実施例 1
クロルメチル化スチレンージビニルベンゼン樹脂10碇
部(0.37モル)へ33礎部の塩化メチレンを加え、
次にこの混合物へ水150部、メタノール320部、お
よびジメチルサルフアィド8.3部(0.137モル)
を加えて室温9錨寿間振燈した。Note that parts in the examples represent parts by weight. Example 1 To 10 parts (0.37 mol) of chloromethylated styrene-divinylbenzene resin, 33 parts of methylene chloride was added,
Next, 150 parts of water, 320 parts of methanol, and 8.3 parts (0.137 mol) of dimethyl sulfide were added to this mixture.
was added and kept at room temperature for 9 hours.
このようにして得られたキレート樹脂を単離して水洗し
、さらにこの樹脂を20Q血のマグネシウムを含む溶液
に浸してキレート官能基末端をマグネシウム型にした。
このマグネシウム型キレート樹脂1部とイオン交換水5
部を1その冷却管付き3つロフラスコに入れ減量する交
換水を添加しつつ90qoで5時間空気を吹き込んだ。The chelate resin thus obtained was isolated and washed with water, and the resin was further immersed in a solution containing 20Q blood magnesium to convert the chelate functional group terminal into a magnesium type.
1 part of this magnesium type chelate resin and 5 parts of ion exchange water
One part was placed in a three-loaf flask equipped with a condenser tube, and air was blown at 90 qo for 5 hours while adding replacement water to reduce the volume.
単離したキレート樹脂には溶媒の臭はなく、またキレー
ト性能を測定したところ処理前と殆ど差が認められなか
った。一方マグネシウムを含む溶液で処理しないで同様
の脱臭処理を施こしたキレート樹脂のキレ−ト性能の低
下は約23%であった。The isolated chelate resin had no solvent odor, and when its chelating performance was measured, there was almost no difference from before treatment. On the other hand, when a chelate resin was subjected to a similar deodorizing treatment without being treated with a magnesium-containing solution, the chelating performance decreased by about 23%.
実施例 2
フェノール系キレート樹脂ュニセレツクUR−10〔フ
ェノール縮合体を樹脂母体とし、官能基としてィミノジ
酢酸を有し、その末端にNa型を有する。Example 2 Phenolic chelate resin UNISEREC UR-10 [The resin base is a phenol condensate, has iminodiacetic acid as a functional group, and has an Na type at its terminal.
ユニチカ■製〕を20功血の銅を含有する水溶液に浸潰
して、キレート官能基末端を銅型にした。このキレート
樹脂1部とイオン交換水5部を実施例1と同様の方法で
脱臭処理したところ、処理樹脂のキレート性能の低下は
殆ど認められなかつた。一方、上記と同様のュニセレッ
クUR−10およびこれを硫酸水溶液で処理してキレー
ト官能基末端をH型としたキレート樹脂を実施例1と同
様の夕方法で脱臭処理したところ、Na型キレート樹脂
のキレート性能の低下は約50%であり、H型キレート
樹脂のそれは約20%であった。[manufactured by Unitika ■] was soaked in an aqueous solution containing 20-gold copper to make the end of the chelate functional group into a copper type. When 1 part of this chelate resin and 5 parts of ion-exchanged water were deodorized in the same manner as in Example 1, almost no decrease in the chelating performance of the treated resin was observed. On the other hand, when the same UNICEREC UR-10 as above and the chelate resin which was treated with an aqueous sulfuric acid solution to make the chelate functional group terminal H-type were deodorized in the same manner as in Example 1, it was found that the Na-type chelate resin The decrease in chelating performance was about 50%, and that of the H-type chelate resin was about 20%.
Claims (1)
水に浸漬して該樹脂内部に残留する溶媒およびモノマー
等の不純物を洗浄除去することを特徴とするキレート樹
脂の脱臭法。 2 熱水が80℃以上のものである特許請求の範囲第1
項記載の脱臭法。 3 不純物の洗浄除去が熱水に空気を送風して行なわれ
るものである特許請求の範囲第1項または第2項記載の
脱臭法。 4 不純物の洗浄除去が熱水に加熱水蒸気を吹き込んで
行なわれるものである特許請求の範囲第1項または第2
項記載の脱臭法。[Claims] 1. A method for deodorizing a chelate resin, which comprises exchanging and adsorbing heavy metal ions onto the chelate resin, and then immersing the resin in hot water to wash and remove impurities such as solvents and monomers remaining inside the resin. . 2 Claim 1 in which the hot water is of 80°C or higher
Deodorization method described in section. 3. The deodorizing method according to claim 1 or 2, wherein the cleaning and removal of impurities is carried out by blowing air through hot water. 4. Claim 1 or 2, in which impurities are washed and removed by blowing heated steam into hot water.
Deodorization method described in section.
Priority Applications (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
JP3298077A JPS6010521B2 (en) | 1977-03-24 | 1977-03-24 | Chelate resin deodorization method |
Applications Claiming Priority (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
JP3298077A JPS6010521B2 (en) | 1977-03-24 | 1977-03-24 | Chelate resin deodorization method |
Publications (2)
Publication Number | Publication Date |
---|---|
JPS53117082A JPS53117082A (en) | 1978-10-13 |
JPS6010521B2 true JPS6010521B2 (en) | 1985-03-18 |
Family
ID=12374018
Family Applications (1)
Application Number | Title | Priority Date | Filing Date |
---|---|---|---|
JP3298077A Expired JPS6010521B2 (en) | 1977-03-24 | 1977-03-24 | Chelate resin deodorization method |
Country Status (1)
Country | Link |
---|---|
JP (1) | JPS6010521B2 (en) |
Families Citing this family (1)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
JPS5573705A (en) * | 1978-11-28 | 1980-06-03 | Miyoshi Oil & Fat Co Ltd | Metal-adsorbable chelate resin having deodorizing property |
-
1977
- 1977-03-24 JP JP3298077A patent/JPS6010521B2/en not_active Expired
Also Published As
Publication number | Publication date |
---|---|
JPS53117082A (en) | 1978-10-13 |
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