JPH0144117B2 - - Google Patents
Info
- Publication number
- JPH0144117B2 JPH0144117B2 JP20628383A JP20628383A JPH0144117B2 JP H0144117 B2 JPH0144117 B2 JP H0144117B2 JP 20628383 A JP20628383 A JP 20628383A JP 20628383 A JP20628383 A JP 20628383A JP H0144117 B2 JPH0144117 B2 JP H0144117B2
- Authority
- JP
- Japan
- Prior art keywords
- aqueous solution
- electrolyte
- chromium
- chromium compounds
- concentration
- 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
- 239000003792 electrolyte Substances 0.000 claims description 35
- 150000001845 chromium compounds Chemical class 0.000 claims description 31
- 239000007864 aqueous solution Substances 0.000 claims description 30
- 239000011347 resin Substances 0.000 claims description 17
- 229920005989 resin Polymers 0.000 claims description 17
- 239000013522 chelant Substances 0.000 claims description 16
- 238000000034 method Methods 0.000 claims description 13
- DKVNPHBNOWQYFE-UHFFFAOYSA-N carbamodithioic acid Chemical compound NC(S)=S DKVNPHBNOWQYFE-UHFFFAOYSA-N 0.000 claims description 2
- BUZRUIZTMOKRPB-UHFFFAOYSA-N carboxycarbamic acid Chemical compound OC(=O)NC(O)=O BUZRUIZTMOKRPB-UHFFFAOYSA-N 0.000 claims description 2
- 125000003396 thiol group Chemical class [H]S* 0.000 claims description 2
- 125000000524 functional group Chemical group 0.000 claims 1
- XLYOFNOQVPJJNP-ZSJDYOACSA-N Heavy water Chemical compound [2H]O[2H] XLYOFNOQVPJJNP-ZSJDYOACSA-N 0.000 description 16
- 239000011651 chromium Substances 0.000 description 7
- 239000007788 liquid Substances 0.000 description 7
- VYZAMTAEIAYCRO-UHFFFAOYSA-N Chromium Chemical compound [Cr] VYZAMTAEIAYCRO-UHFFFAOYSA-N 0.000 description 5
- 229910052804 chromium Inorganic materials 0.000 description 5
- 239000008151 electrolyte solution Substances 0.000 description 4
- 239000000243 solution Substances 0.000 description 4
- XLYOFNOQVPJJNP-UHFFFAOYSA-N water Substances O XLYOFNOQVPJJNP-UHFFFAOYSA-N 0.000 description 4
- KRVSOGSZCMJSLX-UHFFFAOYSA-L chromic acid Substances O[Cr](O)(=O)=O KRVSOGSZCMJSLX-UHFFFAOYSA-L 0.000 description 2
- JOPOVCBBYLSVDA-UHFFFAOYSA-N chromium(6+) Chemical class [Cr+6] JOPOVCBBYLSVDA-UHFFFAOYSA-N 0.000 description 2
- 238000004140 cleaning Methods 0.000 description 2
- 230000003247 decreasing effect Effects 0.000 description 2
- AWJWCTOOIBYHON-UHFFFAOYSA-N furo[3,4-b]pyrazine-5,7-dione Chemical compound C1=CN=C2C(=O)OC(=O)C2=N1 AWJWCTOOIBYHON-UHFFFAOYSA-N 0.000 description 2
- LEQAOMBKQFMDFZ-UHFFFAOYSA-N glyoxal Chemical compound O=CC=O LEQAOMBKQFMDFZ-UHFFFAOYSA-N 0.000 description 2
- KXDHJXZQYSOELW-UHFFFAOYSA-N Carbamic acid Chemical compound NC(O)=O KXDHJXZQYSOELW-UHFFFAOYSA-N 0.000 description 1
- 229910000599 Cr alloy Inorganic materials 0.000 description 1
- 239000002253 acid Substances 0.000 description 1
- 230000002378 acidificating effect Effects 0.000 description 1
- 239000000788 chromium alloy Substances 0.000 description 1
- 239000012141 concentrate Substances 0.000 description 1
- 238000011033 desalting Methods 0.000 description 1
- 238000005868 electrolysis reaction Methods 0.000 description 1
- 239000011521 glass Substances 0.000 description 1
- 229940015043 glyoxal Drugs 0.000 description 1
- 229910001385 heavy metal Inorganic materials 0.000 description 1
- 239000000463 material Substances 0.000 description 1
- 229910052751 metal Inorganic materials 0.000 description 1
- 239000002184 metal Substances 0.000 description 1
- 239000000203 mixture Substances 0.000 description 1
- 230000007935 neutral effect Effects 0.000 description 1
- 230000000704 physical effect Effects 0.000 description 1
- 229920001467 poly(styrenesulfonates) Polymers 0.000 description 1
- 229920000768 polyamine Polymers 0.000 description 1
- 238000001556 precipitation Methods 0.000 description 1
- 150000003839 salts Chemical class 0.000 description 1
- 238000004062 sedimentation Methods 0.000 description 1
- 239000000126 substance Substances 0.000 description 1
- 230000007704 transition Effects 0.000 description 1
- 238000005406 washing Methods 0.000 description 1
- 238000004065 wastewater treatment Methods 0.000 description 1
Landscapes
- Treatment Of Water By Ion Exchange (AREA)
Description
【発明の詳細な説明】
本発明は、アルカリ性の電解質水溶液中に極微
量存在するクロム化合物をキレート樹脂によつ
て、上記電解質水溶液のPHおよび電解質濃度を変
化させることなくクロム化合物のみを除去する方
法に関する。DETAILED DESCRIPTION OF THE INVENTION The present invention provides a method for removing only chromium compounds present in trace amounts in an alkaline electrolyte aqueous solution using a chelate resin without changing the pH and electrolyte concentration of the electrolyte aqueous solution. Regarding.
従来、微量のクロム化合物の除去は、排水処理
等においても広く行なわれているが、いずれもPH
の変動、薬剤の添加を伴いクロム化合物を除去し
た後の水溶液の性質は大幅に変化する。また水溶
液がアルカリ性の場合、3価のクロム化合物は沈
澱除去されるが、数ppmまでの除去が限界であ
る。 Conventionally, the removal of trace amounts of chromium compounds has been widely carried out in wastewater treatment, etc., but in both cases PH
The properties of the aqueous solution after removing the chromium compounds change significantly with the addition of chemicals. Furthermore, when the aqueous solution is alkaline, trivalent chromium compounds can be removed by precipitation, but the removal is limited to a few ppm.
ところでアルカリ性電解質水溶液中にクロム化
合物が存在する系を電解すると、電解の過電圧が
変化する等の障害が発生することがある。このた
め、クロム化合物を経時的に除去しなければなら
ないが、一般に行なわれているクロム除去法で
は、電解質水溶液のPH、電解質濃度の変化を避け
得なかつた。特に電解質水溶液中には3価および
6価のクロム化合物が共存することが多く、6価
クロム化合物の溶解度は大きく、電解質水溶液の
組成および物性を変えずにクロム化合物を充分除
去する方法がなかつた。 However, when a system in which a chromium compound is present in an alkaline electrolyte aqueous solution is electrolyzed, problems such as a change in the electrolytic overvoltage may occur. For this reason, the chromium compound must be removed over time, but in the commonly used chromium removal method, changes in the pH and electrolyte concentration of the electrolyte aqueous solution cannot be avoided. In particular, trivalent and hexavalent chromium compounds often coexist in electrolyte aqueous solutions, and the solubility of hexavalent chromium compounds is high, so there has been no method to sufficiently remove chromium compounds without changing the composition and physical properties of electrolyte aqueous solutions. .
本発明者らは上記の事情に鑑み、鋭意研究した
結果、一般に中性ないし酸性で使用されるCr、
Crの除去用キレート樹脂を用いて、アルカリ
性の電解質水溶液中のクロム化合物を、上記水溶
液のPH、電解質濃度を物性を変えずに、極低濃度
まで除去することが出来ることを発見した。その
要旨は、クロム化合物を含有するアルカリ性の電
解質水溶液と同じ電解質濃度およびPHを有する水
溶液によつて処理したキレート樹脂に、上記クロ
ム化合物を含有するアルカリ性の電解質水溶液を
通液し微量のクロム化合物を除去することを特徴
とする電解質水溶液中のクロム化合物の除去法に
ある。 In view of the above circumstances, the present inventors conducted extensive research and found that Cr, which is generally used in a neutral or acidic state,
We have discovered that it is possible to remove chromium compounds in an alkaline electrolyte aqueous solution to an extremely low concentration without changing the pH or electrolyte concentration of the aqueous solution by using a chelate resin for removing Cr. The gist is that an alkaline aqueous electrolyte solution containing a chromium compound is passed through a chelate resin that has been treated with an aqueous solution having the same electrolyte concentration and pH as the aqueous alkaline electrolyte solution containing a chromium compound, and a trace amount of the chromium compound is removed. A method for removing chromium compounds in an electrolyte aqueous solution is provided.
以下本発明を説明する。 The present invention will be explained below.
本発明に使用されるキレート樹脂としては、ア
ミノカルボン酸を配位基とするもの(例えば
Dowex A−1)、ポリアミンを配位基とするも
の、或いはグリオキザールビスヒドロキシアニ
ル、イミノカルボン酸、イミノジカルボン酸、ジ
チオカルバミン酸、チオール等またはその金属塩
を配位基とするものがあるが、その他2価以上の
遷移重金属を取込むキレート樹脂も使用可能であ
る。 As the chelate resin used in the present invention, those having an aminocarboxylic acid as a coordination group (for example,
Dowex A-1), some have polyamine as a coordinating group, others have glyoxal bishydroxyanyl, iminocarboxylic acid, iminodicarboxylic acid, dithiocarbamic acid, thiol, etc. or a metal salt thereof as a coordinating group, but there are others. Chelate resins that incorporate divalent or higher transition heavy metals can also be used.
上記キレート樹脂は、一般に純水溶液で合成さ
れ、脱塩操作を行なつた後純水中に保持される。
したがつて、そのままアルカリ性の電解質水溶液
中のクロム化合物除去に使用すると、クロム化合
物を除去したあとの電解質水溶液のPHおよび電解
質濃度が変化する。そのため、上記電解質水溶液
とPHおよび電解質濃度が同じ水溶液によつて、上
記キレート樹脂を洗浄した後クロム化合物を含有
する電解質水溶液中のクロム化合物除去に使用す
る。この操作によつて、PHおよび電解質濃度を変
化させないでクロム化合物を除去することが可能
となる。 The above-mentioned chelate resin is generally synthesized in a pure water solution, and after a desalting operation is carried out, it is kept in pure water.
Therefore, if it is used as it is to remove chromium compounds from an alkaline electrolyte aqueous solution, the pH and electrolyte concentration of the electrolyte aqueous solution will change after the chromium compounds are removed. Therefore, the chelate resin is washed with an aqueous solution having the same pH and electrolyte concentration as the aqueous electrolyte solution, and then used to remove chromium compounds from the aqueous electrolyte solution containing chromium compounds. This operation makes it possible to remove chromium compounds without changing the pH and electrolyte concentration.
キレート樹脂によるクロム化合物の除去法には
種々な方法があるが、通常、キレート樹脂を充填
塔に充填し、クロム化合物を含有する電解質水溶
液(以下被処理液という)と、PHおよび電解質濃
度が同じ水溶液を予め流通せしめて洗浄を行な
い、しかる後被処理液を流通せしめてクロム化合
物を除去する。 There are various methods for removing chromium compounds using chelate resin, but usually the chelate resin is packed into a packed tower and the chromium compound-containing electrolyte aqueous solution (hereinafter referred to as the liquid to be treated) has the same pH and electrolyte concentration. Washing is performed by flowing an aqueous solution in advance, and then the chromium compound is removed by flowing a liquid to be treated.
上記方法はクロム合金材料によつてつくられた
装置を用いたプラントの液中に溶出する微量のク
ロム化合物を除去して再使用するような系に利用
出来るが、特に重水濃縮に使用する電解槽の電解
質水溶液中のクロム化合物を除去する方法として
優れている。この方法によつて、電解質水溶液は
容易に再使用可能となり、また、クロム化合物を
除去することによつて、電気分解時の過電圧の変
化もなくなり、重水の能率的な濃縮が可能とな
る。 The above method can be used in systems that remove and reuse trace amounts of chromium compounds eluted into liquid in plants using equipment made of chromium alloy materials, but especially in electrolytic tanks used for heavy water concentration. This is an excellent method for removing chromium compounds from electrolyte aqueous solutions. By this method, the electrolyte aqueous solution can be easily reused, and by removing chromium compounds, there is no change in overvoltage during electrolysis, making it possible to efficiently concentrate heavy water.
以下重水電解濃縮装置の電解液中のクロム化合
物除去を例として実施例を示し本発明を具体的に
説明する。 EXAMPLES The present invention will be specifically explained below by way of examples, taking as an example the removal of chromium compounds from the electrolyte of a heavy water electrolytic concentrator.
実施例 1
イミノカルボン酸塩型のキレート樹脂を用い、
次の手順によつてアルカリ性の電解質水溶液中の
クロム化合物の除去を行なつた。先ず、沈降容量
で68mlの上記キレート樹脂を内径30mmのガラス製
カラムに充填し、軽水730mlによつて通水洗浄し
た。次いでこれにPH:12.5およびアルカリ濃度:
8.4wt%、重水/(重水+軽水):93.2wt%の重水
溶液を洗浄液として600ml/hrの流速で280ml流通
し樹脂を洗浄した。Example 1 Using an iminocarboxylate type chelate resin,
The chromium compounds in the alkaline electrolyte aqueous solution were removed by the following procedure. First, the above chelate resin with a sedimentation capacity of 68 ml was packed into a glass column with an inner diameter of 30 mm, and washed with 730 ml of light water. Then add this to PH: 12.5 and alkaline concentration:
8.4 wt% heavy water/(heavy water + light water): 280 ml of a 93.2 wt% heavy water solution was passed as a cleaning liquid at a flow rate of 600 ml/hr to wash the resin.
このキレート樹脂に全クロム濃度0.2ppmを含
有する上記洗浄液と同じPH、および電解質濃度、
および重水濃度の電解質水溶液を被処理液として
600ml/hrの流速で2400ml通液した。キレート樹脂
処理前後におけるPH、電解質濃度および重水濃度
は変化なく、全クロムの含有量のみ0.096ppmに
低下した。 This chelate resin has the same pH and electrolyte concentration as the above cleaning solution containing a total chromium concentration of 0.2 ppm,
and electrolyte aqueous solution with heavy water concentration as the liquid to be treated.
2400 ml of liquid was passed through at a flow rate of 600 ml/hr. The pH, electrolyte concentration, and heavy water concentration before and after chelate resin treatment remained unchanged, and only the total chromium content decreased to 0.096 ppm.
実施例 2
被処理液としてクロム酸濃度3.36ppm(クロム
換算)の電解質水溶液を用い600ml/hrの流速で
2720ml通した外は、実施例1と同じにした。その
結果被処理液の処理前、処理後のPHおよび電解質
濃度は変化なく、クロム酸濃度(クロム換算)の
み0.05ppmに低下した。Example 2 An electrolyte aqueous solution with a chromic acid concentration of 3.36 ppm (chromium equivalent) was used as the liquid to be treated at a flow rate of 600 ml/hr.
The procedure was the same as in Example 1 except that 2720 ml was passed through. As a result, the pH and electrolyte concentration of the treated solution before and after treatment remained unchanged, and only the chromic acid concentration (in terms of chromium) decreased to 0.05 ppm.
Claims (1)
水溶液と同じ電解質濃度およびPHを有する水溶液
によつて処理したキレート樹脂を用いて上記電解
質水溶液中の微量のクロム化合物を除去すること
を特徴とする電解質水溶液中のクロム化合物の除
去法。 2 キレート樹脂がイミノカルボン酸塩、イミノ
ジカルボン酸塩、ジチオカルバミン酸、チオール
を官能基として有するキレート樹脂である特許請
求の範囲第1項記載の電解質水溶液中のクロム化
合物の除去法。 3 クロム化合物を含有するアルカリ性の電解質
水溶液が重水溶液である特許請求の範囲第1項記
載の電解質水溶液中のクロム化合物の除去法。[Claims] 1. A trace amount of chromium compound in the electrolyte aqueous solution is removed using a chelate resin treated with an aqueous solution having the same electrolyte concentration and pH as the alkaline electrolyte aqueous solution containing the chromium compound. A method for removing chromium compounds from an electrolyte aqueous solution. 2. The method for removing chromium compounds in an electrolyte aqueous solution according to claim 1, wherein the chelate resin is a chelate resin having an iminocarboxylate, an iminodicarboxylate, a dithiocarbamic acid, or a thiol as a functional group. 3. The method for removing chromium compounds in an electrolyte aqueous solution according to claim 1, wherein the alkaline electrolyte aqueous solution containing a chromium compound is a heavy aqueous solution.
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| JP20628383A JPS60100699A (en) | 1983-11-02 | 1983-11-02 | Method for removing chromium compound from aqueous electrolyte solution |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| JP20628383A JPS60100699A (en) | 1983-11-02 | 1983-11-02 | Method for removing chromium compound from aqueous electrolyte solution |
Publications (2)
| Publication Number | Publication Date |
|---|---|
| JPS60100699A JPS60100699A (en) | 1985-06-04 |
| JPH0144117B2 true JPH0144117B2 (en) | 1989-09-26 |
Family
ID=16520742
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| JP20628383A Granted JPS60100699A (en) | 1983-11-02 | 1983-11-02 | Method for removing chromium compound from aqueous electrolyte solution |
Country Status (1)
| Country | Link |
|---|---|
| JP (1) | JPS60100699A (en) |
Families Citing this family (1)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| JP5580652B2 (en) * | 2009-04-23 | 2014-08-27 | ローム アンド ハース カンパニー | Reduce the amount of antimicrobial compounds during product distribution |
-
1983
- 1983-11-02 JP JP20628383A patent/JPS60100699A/en active Granted
Also Published As
| Publication number | Publication date |
|---|---|
| JPS60100699A (en) | 1985-06-04 |
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