JPS6046042B2 - Method for producing iodine from natural can water - Google Patents
Method for producing iodine from natural can waterInfo
- Publication number
- JPS6046042B2 JPS6046042B2 JP52086488A JP8648877A JPS6046042B2 JP S6046042 B2 JPS6046042 B2 JP S6046042B2 JP 52086488 A JP52086488 A JP 52086488A JP 8648877 A JP8648877 A JP 8648877A JP S6046042 B2 JPS6046042 B2 JP S6046042B2
- Authority
- JP
- Japan
- Prior art keywords
- water
- iodine
- natural
- gun water
- sodium hypochlorite
- 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
- Treatment Of Water By Oxidation Or Reduction (AREA)
Description
【発明の詳細な説明】
本発明は、次亜塩素酸ナトリウムを含有する液を用い
て、天然ガン水中のヨウ素イオンを酸化して、ヨウ素を
遊離させ、アニオン交換樹脂等を用いてヨウ素の採取操
作を行うとき、適当量の鉱酸を添加して、ヨウ素の採取
効率を向上させるヨウ素の製造方法に関するものである
。Detailed Description of the Invention The present invention uses a solution containing sodium hypochlorite to oxidize iodine ions in natural gun water to liberate iodine, and then collects iodine using an anion exchange resin or the like. The present invention relates to a method for producing iodine, which improves the efficiency of iodine collection by adding an appropriate amount of mineral acid during the operation.
従来、天然ガン水から、ヨウ素を製造する方法として
塩素、塩素水及び次亜塩素酸塩を酸化剤として用い、天
然ガン水中のヨウ素イオンを分子状ヨウ素として遊離せ
しめ、活性炭、イオン交換樹脂等を吸着させる方法、若
しくは空気追い出しを行う方法等が試みられている。Conventionally, the method for producing iodine from natural cancer water uses chlorine, chlorine water, and hypochlorite as oxidizing agents to liberate the iodine ions in natural cancer water as molecular iodine, and then uses activated carbon, ion exchange resin, etc. Attempts have been made to use methods such as adsorption methods and air expulsion methods.
これらの方法の中で、天然ガン水を鉱酸で酸性とし、
塩素ガス等て酸化する方法は生じた遊離ヨウ素が比較的
安定であり、過酸化物であるヨウ素酸イオンが、生成す
ることもなく活性炭やイオン交換樹脂で、効率的にヨウ
素を吸着採取さすことができるが、天然ガン水を酸性に
するに必要な鉱酸量が多量であり、ヨウ素採取後のガン
水(以下廃ガン水という)を中和するに必要なアルカリ
剤の消費量も大きいという欠点を有している。Among these methods, natural gun water is made acidic with mineral acids;
In the method of oxidizing with chlorine gas, etc., the free iodine produced is relatively stable, and iodine can be efficiently adsorbed and collected using activated carbon or ion exchange resin without producing iodate ions, which are peroxides. However, the amount of mineral acid required to make natural gun water acidic is large, and the amount of alkaline agent required to neutralize the gun water after iodine extraction (hereinafter referred to as waste gun water) is also large. It has its drawbacks.
又、天然ガン水のPHを調整することなく、塩素ガス
を添加する方法は、過酸化物てあるヨウ素酸イオンが1
5%以上発生する。このヨウ素酸イオンの採取は、困難
て殆んどそのまま廃ガン水に移行してしまうので塩素ガ
スを直接天然ガン水に添加する方法は採取効率が低いと
いう欠点を有している。 廃ガン水の一部に塩素ガスを
添加して、塩素より酸化力の弱い塩素水を調整して用い
る場合、ヨウ素酸イオンの発生率は約5%程度となり、
イオン交換樹脂法又は空気追い出し法等に実用的に用い
られている。In addition, the method of adding chlorine gas without adjusting the pH of natural gun water is that the iodate ion in peroxide is
Occurs in 5% or more. It is difficult to collect these iodate ions, and most of the iodate ions are transferred directly to waste gun water, so the method of directly adding chlorine gas to natural gun water has the disadvantage of low collection efficiency. When adding chlorine gas to a portion of waste gun water to prepare chlorine water, which has weaker oxidizing power than chlorine, the generation rate of iodate ions is approximately 5%.
It is practically used in ion exchange resin method, air expulsion method, etc.
しかしながら、この方法の場合、有効塩素濃度を高く
すると、ヨウ素酸イオンの発生率が高くなるので、通常
塩素として1ダ/1−カン水以下に調整されて用いてい
る。However, in the case of this method, when the effective chlorine concentration is increased, the generation rate of iodate ions increases, so the chlorine used is usually adjusted to 1 da/1-kan water or less.
従つて、塩素水を調整する水量が膨大であり、通常廃
ガン水の一部が用いられるも、この水量は採取処理しよ
うとするヨウ素イオンを含む天然ガン水(以下原ガン水
という)の水量の約5%にもなり、採取操作の効率を低
下させる欠点を有している。Therefore, the amount of water required to adjust the chlorinated water is enormous, and although a portion of waste gun water is normally used, this amount of water is equal to the amount of natural cancer water containing iodine ions (hereinafter referred to as raw cancer water) that is to be collected and processed. It has the disadvantage of reducing the efficiency of collection operations.
又廃ガン水を用いて調整する結果、廃ガン水中に含まれ
るアンモニアイオン等に塩素が消費され、原ガン水中の
ヨウ素イオンに対して、理論的に必要な塩素量の約1ゐ
倍乃至3.@もの塩素量を必要とする欠点を有している
。又、塩素は劇物であり100%の安全管理を必要とす
る。In addition, as a result of adjustment using waste gun water, chlorine is consumed by ammonia ions, etc. contained in the waste gun water, and the amount of chlorine is approximately 1 to 3 times the theoretically required amount of iodine ions in the original gun water. .. It has the disadvantage of requiring a large amount of chlorine. In addition, chlorine is a hazardous substance and requires 100% safety management.
即ち常時、危険性を内包している。これに対して、次亜
塩素酸ナトリウム液は塩素水より酸化力が弱く分解して
発生する気体は酸素なので安全性が高く、市販の有効塩
素12%の次亜塩素酸ナトリウム液をそのまま用いるこ
とができるので、その添加量は原ガン水量の約0.03
%の程度の液量となりヨウ素採取操作の効率は100%
近くになる有利性を有している。本発明は、上記の塩素
水の欠点を除き次亜塩素酸ナトリウムを含む液の有利性
を実用化したものてある。In other words, there is always a danger involved. On the other hand, sodium hypochlorite solution has weaker oxidizing power than chlorine water, and the gas generated when it decomposes is oxygen, so it is highly safe, so commercially available sodium hypochlorite solution with 12% available chlorine can be used as is. Therefore, the amount added is approximately 0.03 of the amount of raw gun water.
%, and the efficiency of the iodine collection operation is 100%.
It has the advantage of being close. The present invention has put into practical use the advantages of a solution containing sodium hypochlorite, while eliminating the disadvantages of chlorinated water.
次亜塩素酸ナトリウムを含む液を用いることのもう一つ
の有利性はヨウ素酸イオンの発生率が2%以下で天然ガ
ン水中のヨウ素イオンを100%近く採取できる可能性
を有していることである。Another advantage of using a solution containing sodium hypochlorite is that the generation rate of iodate ions is less than 2%, making it possible to extract nearly 100% of the iodine ions in natural gun water. be.
このヨウ素酸イオンの発生率は、次亜塩素酸ナトリウム
の有効塩素濃度に左右されるものではなく、天然ガン水
に添加したときの攪拌混合条件に左右されるものてある
。しかしながら、次亜塩素酸ナトリウムを含む液を用い
てヨウ素を遊離させた場合、塩素水の場合と比較して表
−1に示すように分解が早い。The rate of generation of iodate ions does not depend on the effective chlorine concentration of sodium hypochlorite, but rather on the stirring and mixing conditions when added to natural gun water. However, when iodine is liberated using a solution containing sodium hypochlorite, the decomposition is faster than in the case of chlorine water, as shown in Table 1.
ヨウ素採取操作の処理時間を短くすれは経時変化は少量
になり問題とならないと観られようが、ヨウ素採取操作
時に本質的な相異が両者にあるこL.JOVIl7,日
nセ 祠ゴ害→レn)t巳ノト 広hソ7P6)D
■′→次亜塩素酸ナトリウム液の場合は、逆に極く僅少
であるがPHは上昇する。このようなPH上昇は市販の
有効塩素濃度12%の次亜塩素酸ナトリウム液を用いた
場合だけでなく、海水、廃ガン水、食塩水等を用いて無
隔膜電解によつて生じる次亜塩素酸ナトリウムを含む液
や、隔膜電解によつて生じた陰極液と陽極液とを合せて
生じる次亜塩素酸ナトリウムを含む液を使用した場合に
も同様な現象が生じる。この現象は、酸化反応で副生す
る水酸化ナトリウムが主因であり、ヨウ素採取操作を妨
害するものと思われる。If the processing time of the iodine collection operation is shortened, the change over time will be small and not a problem, but there is an essential difference between the two in the iodine collection operation. JOVIl7, day nse Shrine Go Harm → Ren) t Mi no To Hiroh So 7P6) D
■'→In the case of sodium hypochlorite solution, on the other hand, the pH increases, albeit very slightly. Such a pH increase occurs not only when using a commercially available sodium hypochlorite solution with an effective chlorine concentration of 12%, but also when hypochlorite is generated by non-diaphragm electrolysis using seawater, waste gun water, salt water, etc. A similar phenomenon occurs when a solution containing sodium chloride or a solution containing sodium hypochlorite produced by combining the catholyte and anolyte produced by diaphragm electrolysis are used. This phenomenon is mainly caused by sodium hydroxide, a by-product of the oxidation reaction, which seems to interfere with the iodine extraction operation.
次亜塩素酸ナトリウムを含む液で、天然ガン水中のヨウ
素イオンを酸化して、ヨウ素を適当量遊離せしめたガン
水(以下反応ガン水という)を陰イオン交換樹脂例えば
アンパーライトIRA−400(商品名)を充填した塔
に通液して、ヨウ素を採取しようとした場合、塩素水を
用いた場合と比較すると著しく吸着効果が低く、実用的
価値が低下する。即ち、塩素水の場合、通常、吸着収率
は90%乃至95%の範囲で得られるに対して、次亜塩
素酸ナトリウムの場合は80%乃至85%と約10%の
差があるようにみられる。本発明者は天然ガン水に適当
量の鉱酸を添加することによりこの障害を防止し、次亜
塩素酸ナトリウムが酸化剤として実用的に用いることが
できることを見出した。The iodine ions in natural gun water are oxidized with a solution containing sodium hypochlorite to liberate an appropriate amount of iodine (hereinafter referred to as reaction gun water). If you try to collect iodine by passing the liquid through a column filled with chlorine, the adsorption effect will be significantly lower than when using chlorinated water, and its practical value will decrease. That is, in the case of chlorinated water, the adsorption yield is usually obtained in the range of 90% to 95%, whereas in the case of sodium hypochlorite, the adsorption yield is 80% to 85%, which is about a 10% difference. Be looked at. The present inventor has discovered that this problem can be prevented by adding an appropriate amount of mineral acid to natural gun water, and that sodium hypochlorite can be practically used as an oxidizing agent.
天然ガン水に鉱酸を添加する方法は、次亜塩素酸ナトリ
ウムを含む液を、天然ガン水に添加する前でも、後でも
良く、又同時に添加しても良い。The mineral acid may be added to the natural gun water before or after adding the solution containing sodium hypochlorite to the natural gun water, or it may be added at the same time.
鉱酸の添加量は、使用する次亜塩素酸ナトリウムを含む
液に起因するアルカリ量を中和し、尚かつ、ガン水のP
Hを0.1以上低下せしめるに必要な量が望ましい。即
ち(原ガン水のPH)−(廃ガン水のPH)≧0.1て
あることてある。The amount of mineral acid added is determined to neutralize the amount of alkali caused by the solution containing sodium hypochlorite used, and to reduce the P of gun water.
The amount necessary to reduce H by 0.1 or more is desirable. That is, (PH of raw gun water) - (PH of waste gun water)≧0.1.
廃ガン水のPHを原ガン水のPHより1.0以上低下せ
しめても、鉱酸の使用量が増加するたけて、比例的にヨ
ウ素の採取効率が向上するというわけではないので、鉱
酸の添加量゛は1.0≧(原ガン水PH)−(廃ガン水
PH)≧0.1の範囲が好ましい。Even if the pH of waste gun water is lowered by 1.0 or more than the pH of raw gun water, the iodine extraction efficiency will not increase proportionally even though the amount of mineral acid used will increase. The amount of addition is preferably in the range of 1.0≧(raw gun water PH)−(waste gun water PH)≧0.1.
但し廃ガン水のPHが中性の範囲を越えない限り鉱酸の
添加量を、以上の範囲を越えて添加することを妨げるも
のではない。鉱酸を添加した場合の各ガン水のPH変化
の一例を表−2に示す。(注)
廃ガン水はアンパーライトIRA−400でヨウ素を採
取後のガン水。However, as long as the pH of the waste gun water does not exceed the neutral range, this does not preclude adding the mineral acid in an amount exceeding the above range. An example of the PH change of each gun water when mineral acid is added is shown in Table 2. (Note) Waste gun water is gun water after iodine has been collected using Amperlite IRA-400.
12%次亜塩素酸ナトリウム液の添加量は、原ガン水1
dあたり250mtである。The amount of 12% sodium hypochlorite solution added is 1
250 mt per d.
この鉱酸添加の方法は市販の有効塩素濃度12%次亜塩
素酸ナトリウムを用いる場合にも、又如何なる次亜塩素
酸ナトリウムを含む液の場合にも適用される。実施例
ヨウ素イオン約90ppmを含む天然ガン水を17T1
/時の流量で、アニオン交換樹脂アンパーライトIRA
−400(商品名)約40e充填せる吸着塔に通液せし
めるに当り、市販の有効塩素濃度12%次亜塩素酸ナト
リウム液を約250mt/時の流量で天然ガン水に添加
して、ガン水中のヨウ素を遊離せしめ、24時間連続通
液した。This mineral acid addition method can be applied to the case where commercially available sodium hypochlorite with an effective chlorine concentration of 12% is used, or to any liquid containing sodium hypochlorite. Example Natural gun water containing about 90 ppm of iodine ions was added to 17T1.
Anion exchange resin Amperlite IRA at a flow rate of /hour
-400 (trade name) Approximately 40e In order to pass the liquid through the adsorption tower, a commercially available sodium hypochlorite solution with an effective chlorine concentration of 12% was added to natural gun water at a flow rate of approximately 250 mt/hour. of iodine was liberated, and the solution was continuously passed for 24 hours.
廃ガン水中のヨウ素含量は、平均14.4ppmであつ
た。即ち、2柵間の吸着収率は平均84.0%であつた
。次に前記の天然ガン水1d/時の流量に70%の硫酸
を90m1/時の割合で添加後、前述の次亜塩素酸ナト
リウム液を同量の250m1/時て添加して、前述の吸
着塔に引き続き2桝間連続通液した。The average iodine content in the waste gun water was 14.4 ppm. That is, the average adsorption yield between the two fences was 84.0%. Next, 70% sulfuric acid was added at a rate of 90 ml/hour to the above-mentioned natural gun water 1 d/hour, and then the above-mentioned sodium hypochlorite solution was added at the same rate of 250 ml/hour, and the above-mentioned adsorption Subsequently, liquid was continuously passed through the tower between two mounds.
Claims (1)
水中のヨウ素を酸化してヨウ素を遊離させ、イオン交換
樹脂法によりヨウ素を吸着させるヨウ素の製造方法にお
いて、上記イオン交換樹脂法を行うに先だち天然カン水
に鉱酸を加え、イオン交換樹脂によるヨウ素吸着後の天
然カン水のpHを原天然カン水のpHより0.1乃至1
.0低くすることを特徴とする天然カン水からのヨウ素
製造方法。1. In a method for producing iodine in which iodine in natural kan water is oxidized using a solution containing sodium hypochlorite to liberate iodine, and iodine is adsorbed by an ion exchange resin method, prior to performing the above ion exchange resin method. Mineral acid is added to natural citrus water, and the pH of the natural citrus water after iodine adsorption by an ion exchange resin is 0.1 to 1 from the pH of the original natural citrus water.
.. A method for producing iodine from natural kansui, characterized by reducing the amount to 0.
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| JP52086488A JPS6046042B2 (en) | 1977-07-19 | 1977-07-19 | Method for producing iodine from natural can water |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| JP52086488A JPS6046042B2 (en) | 1977-07-19 | 1977-07-19 | Method for producing iodine from natural can water |
Publications (2)
| Publication Number | Publication Date |
|---|---|
| JPS5421987A JPS5421987A (en) | 1979-02-19 |
| JPS6046042B2 true JPS6046042B2 (en) | 1985-10-14 |
Family
ID=13888360
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| JP52086488A Expired JPS6046042B2 (en) | 1977-07-19 | 1977-07-19 | Method for producing iodine from natural can water |
Country Status (1)
| Country | Link |
|---|---|
| JP (1) | JPS6046042B2 (en) |
Cited By (1)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| JPH01120638U (en) * | 1988-02-09 | 1989-08-16 |
Families Citing this family (2)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN1331733C (en) * | 2005-05-09 | 2007-08-15 | 浙江大学 | Method of recovering iodine from palygorskite ore |
| JP7232174B2 (en) * | 2019-12-27 | 2023-03-02 | 株式会社 東邦アーステック | Co-production method of iodine and salt |
-
1977
- 1977-07-19 JP JP52086488A patent/JPS6046042B2/en not_active Expired
Cited By (1)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| JPH01120638U (en) * | 1988-02-09 | 1989-08-16 |
Also Published As
| Publication number | Publication date |
|---|---|
| JPS5421987A (en) | 1979-02-19 |
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