JPH05123682A - Treatment of solution containing iron ion - Google Patents

Treatment of solution containing iron ion

Info

Publication number
JPH05123682A
JPH05123682A JP29010591A JP29010591A JPH05123682A JP H05123682 A JPH05123682 A JP H05123682A JP 29010591 A JP29010591 A JP 29010591A JP 29010591 A JP29010591 A JP 29010591A JP H05123682 A JPH05123682 A JP H05123682A
Authority
JP
Japan
Prior art keywords
iron
solution
solution containing
ions
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.)
Pending
Application number
JP29010591A
Other languages
Japanese (ja)
Inventor
Yuzuru Yanagisawa
譲 柳澤
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.)
Toyo Engineering Corp
Original Assignee
Toyo Engineering Corp
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 Toyo Engineering Corp filed Critical Toyo Engineering Corp
Priority to JP29010591A priority Critical patent/JPH05123682A/en
Publication of JPH05123682A publication Critical patent/JPH05123682A/en
Pending legal-status Critical Current

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  • Removal Of Specific Substances (AREA)

Abstract

PURPOSE:To efficiently and economically remove iron from a soln. contg. iron ions by a treatment without heating the soln. CONSTITUTION:A soln. contg. at least iron ions as metal ions is acidified to pH< 7 with nitric acid, air is blown into the soln. and the iron ions in the soln. are precipitated and removed by adjusting the soln. to pH >=7 with alkali.

Description

【発明の詳細な説明】Detailed Description of the Invention

【0001】[0001]

【産業上の利用分野】本発明は、金属イオンとして少く
とも鉄イオンを含む溶液から鉄分を沈澱除去する溶液の
処理方法に関する。
BACKGROUND OF THE INVENTION 1. Field of the Invention The present invention relates to a method of treating an iron solution by precipitating and removing iron from a solution containing at least iron ions as metal ions.

【0002】[0002]

【従来の技術】鉄等の金属イオンを含む溶液をpH7以
上にしてから加熱処理をして鉄分を水酸化物として沈澱
分離する方法はよく知られている。その際に、鉄イオン
のほか種々の陽、陰イオンが存在すると、たとえ加熱処
理を経ても前述の沈澱分離を効率的に行うことが出来な
いこともよく知られている。
2. Description of the Related Art A method is well known in which a solution containing a metal ion such as iron is adjusted to pH 7 or more and then heat-treated to precipitate and separate iron as hydroxide. At that time, it is also well known that the presence of various cations and anions in addition to iron ions makes it impossible to efficiently carry out the above-mentioned precipitation separation even if heat treatment is performed.

【0003】加熱処理を経た金属イオンとして少くとも
鉄イオンが存在する溶液が生じる例としては、濃縮器、
乾燥器等の洗浄廃液がある。
Examples of a solution in which at least iron ions are present as metal ions that have undergone heat treatment are a concentrator,
There is waste liquid for cleaning the dryer.

【0004】濃縮器において、鉄のスケールが表面に付
着すると伝熱係数が減少するため、定期的に酸で化学洗
浄したり物理的にスケールを剥したりしてその性能を復
活させている。乾燥器についても同様である。このとき
加熱処理を経た金属イオンとして少くとも鉄イオンを含
む多量の酸性廃液が発生し、これを中和後静置すると沈
澱物と上澄み液に分かれる。この上澄み液は鉄イオンの
沈澱が不十分で着色しており、このままでは排水として
放出できない。この上澄み液から鉄分等を分離する方法
として、次の方法が用いられている。即ち、従来技術で
は加熱器、熱交換器等の加熱源を用いて廃液を沸点近傍
の温度に加熱処理後、アルカリ処理をして鉄分を含む沈
澱物と上澄み液に分離している。
In the concentrator, since the heat transfer coefficient decreases when iron scale adheres to the surface, the performance is revived by periodically performing chemical cleaning with acid or physically removing the scale. The same applies to the dryer. At this time, a large amount of acidic waste liquid containing at least iron ions as metal ions that have undergone the heat treatment is generated, and when neutralized and left to stand, it is separated into a precipitate and a supernatant liquid. The supernatant liquid is colored due to insufficient precipitation of iron ions and cannot be discharged as waste water as it is. The following method is used as a method for separating iron and the like from the supernatant. That is, in the prior art, the waste liquid is heated to a temperature near the boiling point using a heating source such as a heater or a heat exchanger, and then alkali-treated to separate the precipitate containing iron and the supernatant.

【0005】また、鉄イオンが存在する溶液を沈澱処理
する例として、ウランを含む溶液に、鉄イオン及びアル
カリを添加して水酸化物として、ウランを沈澱濾過する
方法がある。鉄イオン及びアルカリを添加するのは、鉄
の水酸化物にウランを共沈させるためである。この方法
においても、沈澱物の濾過性をよくするため、加熱処理
を行っている。
Further, as an example of the precipitation treatment of a solution containing iron ions, there is a method in which iron ions and an alkali are added to a solution containing uranium to form hydroxides to precipitate and filter uranium. The reason for adding the iron ion and the alkali is to coprecipitate uranium in the hydroxide of iron. Also in this method, heat treatment is performed in order to improve the filterability of the precipitate.

【0006】[0006]

【発明が解決しようとする課題】いずれの例において
も、最終的には排出する溶液を加熱後沈澱処理を行い冷
却するという方法を用いており、結果的には無駄な熱エ
ネルギーを消費していることになる。
In each of the examples, a method of finally heating the solution to be discharged and then performing a precipitation treatment and then cooling is used. As a result, wasteful heat energy is consumed. Will be there.

【0007】本発明が解決しようとする課題は、鉄イオ
ンまたは鉄イオンと他のイオンを含む大量の溶液から、
その溶液を加熱することなく、効率的に、経済的に鉄分
を除去する処理方法を提供することにある。
The problem to be solved by the present invention is to solve the problem of a large amount of solution containing iron ions or iron ions and other ions.
An object of the present invention is to provide a treatment method for efficiently and economically removing iron without heating the solution.

【0008】[0008]

【課題を解決するための手段】上記従来技術の有する課
題の解決を図るべく、発明者は鋭意検討を行って本発明
を完成するに至った。
In order to solve the problems of the above-mentioned prior art, the inventor has conducted extensive studies and completed the present invention.

【0009】本発明は、金属イオンとして少くとも鉄イ
オンを含む溶液をpH7未満の硝酸酸性にしたのち、そ
の溶液に空気を吹き込み、次いでアルカリを用いて前記
溶液をpH7以上にすることにより、溶液中の鉄分を沈
澱除去することを特徴としている。
According to the present invention, a solution containing at least iron ions as metal ions is acidified with nitric acid having a pH of less than 7, then air is blown into the solution, and then the solution is adjusted to pH 7 or more by using an alkali to form a solution. It is characterized by removing the iron content in the precipitate.

【0010】本発明で使用する酸は硝酸である。例えば
硫酸酸性や塩酸酸性の溶液では苛性ソーダ等で中和後、
硝酸酸性にするのがよい。その際のpHは7未満であれ
ばよいが、空気吹き込み時間を短くするのに、即ち、特
に速やかに酸化するにはpHは低いほどよく4以下が望
ましい。
The acid used in the present invention is nitric acid. For example, in the case of sulfuric acid acid or hydrochloric acid acid solution, after neutralizing with caustic soda,
It is good to use nitric acid. The pH at that time may be less than 7, but in order to shorten the air blowing time, that is, in order to oxidize particularly quickly, the lower the pH, the better, and the pH is preferably 4 or less.

【0011】空気は、溶液を硝酸酸性にしてから吹き込
む。吹き込み時間は溶液の種類、pH、吹込み器の形状
によっても異なり、溶液1m3 当り2ないし60分であ
り、その吹き込み量は溶液の性状、特に鉄イオンの含有
量によって異なる。吹き込み器の形状は、吹き込み時間
を短くするためには空気が均一に分散する形状が特に望
ましい。空気はアルカリ性で吹き込んでも、後記する比
較例2に示すように、処理能力が硝酸酸性よりおとる。
Air is blown after acidifying the solution with nitric acid. The blowing time varies depending on the type of the solution, the pH, and the shape of the blower, and is 2 to 60 minutes per 1 m 3 of the solution, and the blowing amount varies depending on the properties of the solution, particularly the iron ion content. The shape of the blower is preferably a shape in which air is uniformly dispersed in order to shorten the blowing time. Even if air is blown in as alkaline, as shown in Comparative Example 2 described later, the treatment capacity is lower than that of nitric acid.

【0012】以下、実施例を示すが、本発明はこれに制
限されるものではない。
Examples will be shown below, but the present invention is not limited thereto.

【0013】データを示す下記の表1は100mlメス
シリンダーによる沈降試験結果を示したもので、表中の
沈澱物相と上澄み液相の数値はメスシリンダーの目盛
(高さ)mlを表わす。
The following Table 1 showing the data shows the results of the sedimentation test using a 100 ml measuring cylinder, and the numerical values of the precipitate phase and the supernatant liquid phase in the table represent the scale (height) ml of the measuring cylinder.

【0014】[0014]

【実施例】【Example】

実施例1 加熱処理を経た金属イオンとして少くとも鉄イオンを含
む溶液の例として、鉄2000ppm、硝酸ソーダ20
g/l、炭酸ソーダ5g/l、ヨウ化ソーダ5g/l、
亜硝酸ソーダ5g/lからなるpH7の溶液を調整し
た。容量1000ccのステンレス製オートクレーブに
上記溶液を500ccいれ130℃で60%(wt)ま
で濃縮し、これを取り出す操作をオートクレーブに鉄等
のスケールがつくまで繰り返した。
Example 1 As an example of a solution containing at least iron ions as metal ions that have undergone heat treatment, iron 2000 ppm, sodium nitrate 20
g / l, sodium carbonate 5 g / l, sodium iodide 5 g / l,
A pH 7 solution consisting of 5 g / l of sodium nitrite was prepared. The above solution was put into a stainless steel autoclave having a capacity of 1000 cc and 500 cc was concentrated at 130 ° C. to 60% (wt), and the operation of taking out the solution was repeated until scales such as iron were attached to the autoclave.

【0015】オートクレーブを水洗して付着成分以外の
内容物を別に取り出し、ついで鉄分等のスケールが付着
したオートクレーブを100℃まで昇温した。昇温停止
後に放冷し、5%硝酸溶液100ccを3回にわけて用
い化学洗浄を行った。さらに500ccの水で洗浄し
た。5%硝酸溶液100ccと洗浄水500ccを合わ
せて溶液サンプルとした。このサンプルは黄褐色であっ
た。
The autoclave was washed with water to take out contents other than the adhered components separately, and then the autoclave to which scales such as iron adhered was heated to 100 ° C. After the temperature was stopped, the mixture was allowed to cool, and 100 cc of 5% nitric acid solution was divided into 3 times for chemical cleaning. It was further washed with 500 cc of water. A solution sample was prepared by combining 100 cc of a 5% nitric acid solution and 500 cc of washing water. This sample was yellowish brown.

【0016】上記サンプル600ccに空気ボンベから
300cc/minの速度で約25分空気を供給した
後、苛性ソーダ水溶液でpH7に調整した。
Air was supplied to the above sample 600 cc from an air cylinder at a rate of 300 cc / min for about 25 minutes, and then the pH was adjusted to 7 with a caustic soda aqueous solution.

【0017】その結果、速やかに鉄分を含む沈澱物が沈
降し、上澄み液は透明であった。 実施例2 実施例1のサンプルに実施例1において別に取り出した
付着成分以外の内容物を全量加え、同様の操作をした。
結果は実施例1と同様であった。 比較例1 実施例1の洗浄液を5%硫酸、5%塩酸にかえて同様に
実施した。結果は沈澱が生じなかった。 比較例2 実施例1で先にpHを7にして空気を同様に供給した。
その結果、沈澱は生じたが上澄み液には黄褐色が残って
いた。 実施例3 400g/l硝酸ソーダ水溶液中にウラン、カルシウ
ム、マグネシウム、ニッケル及び鉄イオンの硝酸塩とし
て、それぞれ10、300、300、200および20
0ppmを含むpH3の溶液100ccに実施例1と同
じ条件で空気を吹き込んだ。この溶液を濃苛性ソーダ水
溶液でpH13に調整した後、100mlのメスシリン
ダーに移し、沈降試験を行った。沈降時間と沈澱物の境
界面を測定した結果を表1に示す。
As a result, a precipitate containing iron rapidly settled and the supernatant liquid was transparent. Example 2 To the sample of Example 1, the entire contents other than the adhered components separately taken out in Example 1 were added, and the same operation was performed.
The results were the same as in Example 1. Comparative Example 1 The cleaning liquid of Example 1 was replaced with 5% sulfuric acid and 5% hydrochloric acid, and the same operation was performed. The result was no precipitation. Comparative Example 2 In Example 1, the pH was adjusted to 7 and air was supplied in the same manner.
As a result, precipitation occurred, but a yellowish brown color remained in the supernatant. Example 3 10, 300, 300, 200 and 20, respectively, as nitrates of uranium, calcium, magnesium, nickel and iron ions in a 400 g / l sodium nitrate aqueous solution.
Air was blown into 100 cc of a pH 3 solution containing 0 ppm under the same conditions as in Example 1. This solution was adjusted to pH 13 with a concentrated aqueous solution of sodium hydroxide and then transferred to a 100 ml graduated cylinder for sedimentation test. Table 1 shows the result of measuring the sedimentation time and the boundary surface of the sediment.

【0018】[0018]

【表1】 比較例3 実施例3における空気の吹き込みのかわりに15分間沸
騰させ、常温まで冷却した以外は実施例3と同一の方法
で沈降試験を行った。結果を表1に示す。 比較例4 空気を吹き込まずに実施例3と同じ方法で沈降試験を行
った。結果を表1に示す。上澄み液相中に沈澱物の浮遊
が観測された。
[Table 1] Comparative Example 3 A sedimentation test was performed in the same manner as in Example 3 except that the material was boiled for 15 minutes instead of blowing air in Example 3 and cooled to room temperature. The results are shown in Table 1. Comparative Example 4 A sedimentation test was conducted in the same manner as in Example 3 without blowing air. The results are shown in Table 1. Floating precipitates were observed in the supernatant liquid phase.

【0019】[0019]

【発明の効果】以上説明したように、本発明の鉄イオン
を含む溶液の処理方法によれば、金属イオンとして少く
とも鉄イオンを含む溶液から鉄分を効率的に、経済的に
除去または回収することができ、かつ、鉄イオンを除去
または回収した処理液の再使用も可能である。また、加
熱処理を必要としないので省エネ効果がある。
As described above, according to the method for treating a solution containing iron ions of the present invention, iron is efficiently or economically removed or recovered from a solution containing at least iron ions as metal ions. It is also possible to reuse the treatment liquid from which iron ions have been removed or recovered. Further, there is an energy saving effect because no heat treatment is required.

Claims (1)

【特許請求の範囲】[Claims] 【請求項1】 金属イオンとして少くとも鉄イオンを含
む溶液をpH7未満の硝酸酸性にしたのち、その溶液に
空気を吹き込み、次いでアルカリを用いて前記溶液をp
H7以上にすることにより、溶液中の鉄分を沈澱除去す
ることを特徴とする鉄イオンを含む溶液の処理方法。
1. A solution containing at least iron ions as metal ions is acidified with nitric acid at a pH of less than 7, air is blown into the solution, and then the solution is added with an alkali to p
A method for treating a solution containing iron ions, wherein the content of iron in the solution is removed by precipitation by setting it to H7 or more.
JP29010591A 1991-11-06 1991-11-06 Treatment of solution containing iron ion Pending JPH05123682A (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
JP29010591A JPH05123682A (en) 1991-11-06 1991-11-06 Treatment of solution containing iron ion

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
JP29010591A JPH05123682A (en) 1991-11-06 1991-11-06 Treatment of solution containing iron ion

Publications (1)

Publication Number Publication Date
JPH05123682A true JPH05123682A (en) 1993-05-21

Family

ID=17751865

Family Applications (1)

Application Number Title Priority Date Filing Date
JP29010591A Pending JPH05123682A (en) 1991-11-06 1991-11-06 Treatment of solution containing iron ion

Country Status (1)

Country Link
JP (1) JPH05123682A (en)

Cited By (2)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
KR20030042428A (en) * 2001-11-22 2003-05-28 오르가노 가부시키가이샤 Method for treating power plant heater drain water
JP2009057615A (en) * 2007-09-03 2009-03-19 Nippon Steel Corp Method and facility for removing iron ion from displacement plating liquid

Cited By (2)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
KR20030042428A (en) * 2001-11-22 2003-05-28 오르가노 가부시키가이샤 Method for treating power plant heater drain water
JP2009057615A (en) * 2007-09-03 2009-03-19 Nippon Steel Corp Method and facility for removing iron ion from displacement plating liquid

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