JP2014015649A - Production method of caustic soda - Google Patents

Production method of caustic soda Download PDF

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JP2014015649A
JP2014015649A JP2012152814A JP2012152814A JP2014015649A JP 2014015649 A JP2014015649 A JP 2014015649A JP 2012152814 A JP2012152814 A JP 2012152814A JP 2012152814 A JP2012152814 A JP 2012152814A JP 2014015649 A JP2014015649 A JP 2014015649A
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caustic soda
anode chamber
sodium
electrolysis
acid
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Yasushi Osaki
恭 大崎
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Tosoh Corp
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Abstract

PROBLEM TO BE SOLVED: To provide a production method of caustic soda that is not affected with demand and supply of caustic soda and chlorine because there is not byproduct of chlorine.SOLUTION: In a method in which a sodium salt aqueous solution is subjected to electrolysis by an ion exchange membrane method to produce caustic soda, a hydrogen gas diffusion electrode is used in a positive electrode, caustic soda is generated in a negative electrode chamber, an acid is generated in a positive electrode chamber, the acid is reacted with soda ash and/or sodium bicarbonate to generate a sodium salt to be used in electrolysis.

Description

本発明は、イオン交換膜法によりナトリウム塩水溶液を電気分解して苛性ソーダを製造する方法に関し、塩素と水素を併産することなく、それらのガス成分、特に塩素の需要に影響されることなく苛性ソーダを選択的に製造する方法に関するものである。   The present invention relates to a method for producing caustic soda by electrolyzing an aqueous sodium salt solution by an ion exchange membrane method, and does not co-produce chlorine and hydrogen, and does not affect the demand for their gas components, particularly chlorine. The present invention relates to a method for selectively manufacturing the above.

従来、イオン交換膜法により食塩水を電気分解する苛性ソーダの製造法が工業的に広く実施されており、陽極、陰極、イオン交換膜の改良により、高い電流効率と低電圧化による省エネルギー化も進んでいる。   Conventionally, a manufacturing method of caustic soda that electrolyzes saline by ion exchange membrane method has been widely used industrially, and improvement of anode, cathode, and ion exchange membrane has advanced energy saving by high current efficiency and low voltage. It is out.

一方、従来の電解法では、苛性ソーダとともに塩素および水素を併産するため、特に塩素の需要変動によって苛性ソーダの生産が制約を受けるという課題があった。   On the other hand, in the conventional electrolysis method, since chlorine and hydrogen are produced together with caustic soda, there is a problem that production of caustic soda is restricted particularly by fluctuations in demand for chlorine.

塩素を発生しない苛性ソーダの製造法として、例えば、食塩水の代わりに芒硝水溶液を電気分解する方法が知られている(例えば、特許文献1参照)。芒硝水溶液を用いることにより、塩素は発生しないが、陽極室に硫酸が副生し、陽極室のpHが低下し、苛性ソーダを生成できなくなる、或いは電流効率が低くなるという課題を有していた。また、食塩に比べ芒硝は高コストであるとともに、溶解度が低いため高濃度の電気分解ができないという課題もあった。   As a method for producing caustic soda that does not generate chlorine, for example, a method of electrolyzing a sodium sulfate aqueous solution instead of saline is known (for example, see Patent Document 1). By using an aqueous solution of sodium nitrate, chlorine is not generated, but sulfuric acid is by-produced in the anode chamber, the pH of the anode chamber is lowered, and caustic soda cannot be generated, or current efficiency is lowered. In addition, sodium sulfate is more expensive than salt, and there is a problem that high concentration electrolysis cannot be performed due to low solubility.

特許3196382号公報Japanese Patent No. 3196382

本発明は、イオン交換膜法によりナトウム塩水溶液を電気分解する際に塩素や塩素含有化合物を副生することなく、苛性ソーダのみを製造する方法を提供するものである。   The present invention provides a method for producing only caustic soda without electrolyzing chlorine or a chlorine-containing compound when an aqueous sodium salt solution is electrolyzed by an ion exchange membrane method.

本発明者等は、イオン交換膜法により食塩水を電気分解する苛性ソーダの製造方法について鋭意検討を重ねた結果、陽極に水素ガス拡散電極を用い、陰極室で苛性ソーダを生成し、陽極室で酸を生成させ、該酸をソーダ灰および/または重炭酸ソーダと反応させてナトリウム塩を再生し、それをさらに電気分解することにより、塩素の副生がなく苛性ソーダを製造できることを見出し、本発明を完成するに至った。   As a result of intensive studies on a method for producing caustic soda that electrolyzes saline by an ion exchange membrane method, the present inventors have produced a caustic soda in the cathode chamber using a hydrogen gas diffusion electrode as the anode, and an acid in the anode chamber. And the acid is reacted with soda ash and / or sodium bicarbonate to regenerate the sodium salt, which is further electrolyzed to find that caustic soda can be produced without chlorine by-products, thereby completing the present invention. It came to.

以下、本発明の苛性ソーダの製造方法について説明する。   Hereinafter, the manufacturing method of the caustic soda of this invention is demonstrated.

本発明の電気分解は、イオン交換膜法により食塩水を電気分解する苛性ソーダの製造方法において、陽極に水素ガス拡散電極を使用する。   The electrolysis of the present invention uses a hydrogen gas diffusion electrode as an anode in a method for producing caustic soda that electrolyzes saline by an ion exchange membrane method.

従来の電解法では、金属および/または金属酸化物などの電極が用いられるが、食塩水を原料に用いた場合には、塩素ガスおよび水素ガスが発生していた。それに対して、本発明の方法では水素ガス拡散電極を用いることにより、塩素ガスを発生させず、なおかつ消費エネルギーを低減することができる。   In the conventional electrolysis method, electrodes such as metal and / or metal oxide are used. However, when saline is used as a raw material, chlorine gas and hydrogen gas are generated. On the other hand, in the method of the present invention, chlorine gas is not generated and energy consumption can be reduced by using a hydrogen gas diffusion electrode.

一方、陰極室では通常の電気分解と同様に、苛性ソーダを生成し、電極からは水素が発生する。発生した水素は水素ガス拡散電極に供給する水素(またはその一部)として用いることができる。   On the other hand, in the cathode chamber, caustic soda is generated in the same manner as in normal electrolysis, and hydrogen is generated from the electrodes. The generated hydrogen can be used as hydrogen (or a part thereof) supplied to the hydrogen gas diffusion electrode.

陽極室では酸が発生するが、該酸はソーダ灰および/または重炭酸ソーダと反応させてナトリウム塩を再生させる。再生したナトリウム塩は、さらに電気分解に供給してリサイクルする。   Acid is generated in the anode chamber, which reacts with soda ash and / or sodium bicarbonate to regenerate the sodium salt. The regenerated sodium salt is further recycled for electrolysis.

本発明の方法において、陽極室で発生した酸とソーダ灰および/または重炭酸ソーダとの反応では炭酸ガスが発生するが、本発明の方法で発生する炭酸ガスは極めて高純度かつ高濃度であるため、工業用原料としての価値が高いものである。   In the method of the present invention, carbon dioxide gas is generated in the reaction between the acid generated in the anode chamber and soda ash and / or sodium bicarbonate, but the carbon dioxide gas generated by the method of the present invention is extremely high in purity and concentration. It has high value as an industrial raw material.

本発明の方法において、発生した酸とソーダ灰および/または重炭酸ソーダとの反応は別の反応室で行ってもよいが、ソーダ灰および/または重炭酸ソーダを陽極室に導入することにより、電気分解による酸発生と同時に反応を行って、よりコンパクトな反応装置設計が可能となる。   In the method of the present invention, the reaction between the generated acid and soda ash and / or sodium bicarbonate may be carried out in a separate reaction chamber. However, by introducing soda ash and / or sodium bicarbonate into the anode chamber, A more compact reactor design is possible by reacting simultaneously with generation.

本発明の方法では、ソーダ灰および/または重炭酸ソーダを陽極室に導入することにより、電気分解による酸発生と同時に反応を行う場合には、電解槽内でのスケーリングや電気分解反応への不具合抑止や反応の進行および二酸化炭素の脱気を促進させるため、加温、撹拌することが好ましい。   In the method of the present invention, by introducing soda ash and / or sodium bicarbonate into the anode chamber, when the reaction is carried out simultaneously with the generation of acid by electrolysis, scaling in the electrolytic cell and the suppression of troubles in the electrolysis reaction, In order to promote the progress of the reaction and the degassing of carbon dioxide, it is preferable to warm and stir.

本発明の方法では、陽極室は2≦pH≦6で電気分解することが好ましい。pHが2より小さい領域では陽極室液相側の水素イオンが高濃度となり、カチオン交換膜を通して陰極室側に移動するため、苛性ソーダ生成の電流効率が低下する。また、pHが6を超える領域では中和反応が遅くなり、ソーダ灰および/または重炭酸ソーダや、生成した二酸化炭素が溶液中に残存しやくなる。陽極室のpHは3〜4に調整することが特に好ましい。   In the method of the present invention, the anode chamber is preferably electrolyzed at 2 ≦ pH ≦ 6. In the region where the pH is less than 2, hydrogen ions on the liquid phase side of the anode chamber have a high concentration and move to the cathode chamber side through the cation exchange membrane, so that the current efficiency of caustic soda generation decreases. Further, in the region where the pH exceeds 6, the neutralization reaction is slow, and soda ash and / or sodium bicarbonate and generated carbon dioxide are likely to remain in the solution. The pH of the anode chamber is particularly preferably adjusted to 3-4.

陰極にはガス発生型電極に加え、酸素を導入するガス拡散型電極を用いることができる。またイオン交換膜にはカチオン交換膜が用いられる。電極の材質およびカチオン交換膜は特に限定されないが、従来の電解法による苛性ソーダ製造に用いられているものを用いることができる。   In addition to the gas generating electrode, a gas diffusion electrode that introduces oxygen can be used as the cathode. A cation exchange membrane is used as the ion exchange membrane. The material of the electrode and the cation exchange membrane are not particularly limited, but those used for the production of caustic soda by conventional electrolysis can be used.

本発明の方法によれば、イオン交換膜電解法による苛性ソーダ製造において、塩素、水素を副生せず、それらのガス需給に影響されことなく苛性ソーダが製造できるとともに、電解法におけるエネルギー消費を低減することができる。   According to the method of the present invention, in the production of caustic soda by the ion exchange membrane electrolysis method, it is possible to produce caustic soda without generating chlorine and hydrogen as a by-product and not being affected by the supply and demand of gas, and to reduce energy consumption in the electrolysis method. be able to.

電解槽および外部中和プロセスの概要を示す。An overview of the electrolytic cell and external neutralization process is shown. 電解槽および槽内中和プロセスの概要を示す。An outline of the electrolytic cell and the neutralization process in the cell is shown.

次に、本発明を具体的な実施例で説明するが、本発明はこれらの実施例に限定されるものではない。   Next, although this invention is demonstrated with a specific Example, this invention is not limited to these Examples.

実施例1
陽極として白金を担持した多孔室電極、陰極としてニッケル電極を備え、カチオン交換膜(デユポン社製ナフィオン膜)によって陽極室と陰極室に分離された2室型の電解槽を用いた。陽極室液相側に300g/Lの食塩水を供給し、排出塩水のpHが3になるように流量を調整した。陽極室ガス相側には水素ガスを1L/分の速度で供給した。陰極室へは苛性濃度が30wt%になるように純水を供給しながら、電解電流密度3kA/mで電気分解を実施した。このときの電解電圧は2.4Vであり、苛性ソーダ生成の電流効率は93%であった。
Example 1
A two-chamber electrolytic cell equipped with a porous chamber electrode carrying platinum as an anode and a nickel electrode as a cathode and separated into an anode chamber and a cathode chamber by a cation exchange membrane (Naupion membrane manufactured by Deyupon) was used. 300 g / L saline was supplied to the anode chamber liquid phase side, and the flow rate was adjusted so that the pH of the discharged brine was 3. Hydrogen gas was supplied to the anode chamber gas phase side at a rate of 1 L / min. Electrolysis was performed at an electrolytic current density of 3 kA / m 2 while supplying pure water to the cathode chamber so that the caustic concentration was 30 wt%. The electrolytic voltage at this time was 2.4 V, and the current efficiency of caustic soda generation was 93%.

陽極室から排出された塩酸と食塩水の混合水溶液に、ソーダ灰を添加し、塩酸を中和するとともに、食塩水濃度を300g/Lに調整し、電気分解に再利用した。また、ソーダ灰を添加した時に発生した二酸化炭素は、高純度品として回収した。   Soda ash was added to the mixed aqueous solution of hydrochloric acid and saline discharged from the anode chamber to neutralize the hydrochloric acid and adjust the saline concentration to 300 g / L, which was reused for electrolysis. Carbon dioxide generated when soda ash was added was recovered as a high-purity product.

実施例2
陽極室液相側に250g/Lの芒硝水溶液を供給した以外は、実施例1と同様の条件で電気分解を実施した。このときの電解電圧は2.6Vであり、苛性ソーダ生成の電流効率は90%であった。
Example 2
Electrolysis was carried out under the same conditions as in Example 1 except that 250 g / L of an aqueous sodium silicate solution was supplied to the anode chamber liquid phase side. The electrolytic voltage at this time was 2.6 V, and the current efficiency of caustic soda generation was 90%.

陽極室から排出された硫酸と芒硝の混合水溶液に、ソーダ灰を添加して硫酸を中和するとともに、芒硝水濃度を250g/Lに調整し、電気分解に再利用した。また、ソーダ灰を添加した時に発生した二酸化炭素は、高純度品として回収した。   Soda ash was added to the mixed aqueous solution of sulfuric acid and mirabilite discharged from the anode chamber to neutralize the sulfuric acid, and the concentration of mirabilite water was adjusted to 250 g / L, which was reused for electrolysis. Carbon dioxide generated when soda ash was added was recovered as a high-purity product.

実施例3
実施例1と同様の電解槽を用いて、陽極室液相側に200g/Lの食塩水を張り込んだ。陽極室内の食塩水のpHが6となるようにソーダ灰溶液を供給しながら、実施例1と同様の条件で電気分解を実施した。このときの電解電圧は2.7Vであり、苛性ソーダ生成の電流効率は95%であった。
Example 3
Using the same electrolytic cell as in Example 1, 200 g / L of saline was applied to the anode chamber liquid phase side. Electrolysis was carried out under the same conditions as in Example 1 while supplying a soda ash solution so that the pH of the saline solution in the anode chamber was 6. The electrolytic voltage at this time was 2.7 V, and the current efficiency of caustic soda generation was 95%.

陽極室液側から発生した二酸化炭素は、高純度品として回収した。   Carbon dioxide generated from the anode chamber liquid side was recovered as a high-purity product.

比較例1
排出塩水のpHを1とした以外は、実施例1と同様の条件で実験を行った。このときの電解電圧は2.3Vであり、苛性ソーダ精製の電流効率は75%であった。
Comparative Example 1
The experiment was performed under the same conditions as in Example 1 except that the pH of the discharged salt water was 1. The electrolytic voltage at this time was 2.3 V, and the current efficiency of the caustic soda purification was 75%.

本発明は、塩素を副生しない苛性ソーダの製造に使用することができる。   The present invention can be used to produce caustic soda that does not produce chlorine as a by-product.

Claims (6)

イオン交換膜法によりナトリウム塩水溶液を電気分解して苛性ソーダを製造する方法において、陽極に水素ガス拡散電極を用い、陰極室で苛性ソーダを生成し、陽極室で酸を生成させ、該酸をソーダ灰および/または重炭酸ソーダと反応させてナトリウム塩を生成し、それを電気分解に用いることを特徴とする苛性ソーダの製造方法。 In a method for producing caustic soda by electrolyzing a sodium salt aqueous solution by an ion exchange membrane method, a hydrogen gas diffusion electrode is used as an anode, caustic soda is produced in a cathode chamber, an acid is produced in an anode chamber, and the acid is produced as soda ash. A method for producing caustic soda characterized by reacting with sodium bicarbonate and / or sodium bicarbonate to produce sodium salt, which is used for electrolysis. ソーダ灰および/または重炭酸ソーダと陽極室内において生成する酸の反応を陽極室中で行うことを特徴とする請求項1に記載の苛性ソーダの製造方法。 The method for producing caustic soda according to claim 1, wherein the reaction between the soda ash and / or sodium bicarbonate and the acid generated in the anode chamber is carried out in the anode chamber. 陽極室の電解液を2≦pH≦6で電気分解することを特徴とする請求項1または2記載の苛性ソーダの製造方法。 3. The method for producing caustic soda according to claim 1, wherein the electrolytic solution in the anode chamber is electrolyzed at 2 ≦ pH ≦ 6. ナトリウム塩が、塩化ナトリウムであることを特徴とする請求項1乃至3のいずれか1項に記載の苛性ソーダの製造方法。 The method for producing caustic soda according to any one of claims 1 to 3, wherein the sodium salt is sodium chloride. ナトリウム塩が、硫酸ナトリウムまたは硝酸ナトリウムであることを特徴とする請求項1乃至3のいずれか1項に記載の苛性ソーダの製造方法。 The method for producing caustic soda according to any one of claims 1 to 3, wherein the sodium salt is sodium sulfate or sodium nitrate. 陰極が、酸素ガス拡散電極であることを特徴とする請求項1乃至5のいずれか1項に記載の苛性ソーダの製造方法。 The method for producing caustic soda according to any one of claims 1 to 5, wherein the cathode is an oxygen gas diffusion electrode.
JP2012152814A 2012-07-06 2012-07-06 Production method of caustic soda Pending JP2014015649A (en)

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Cited By (3)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
CN109735868A (en) * 2018-08-26 2019-05-10 熵零技术逻辑工程院集团股份有限公司 A kind of electrolysis unit
KR20220048590A (en) * 2020-10-13 2022-04-20 (주) 테크윈 A DEVICE FOR PRODUCING NaOH AND A DEVICE FOR PRODUCING NaOCl comprising the same
CN116770334A (en) * 2022-03-23 2023-09-19 李枭 Sodium hydroxide production system

Cited By (5)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
CN109735868A (en) * 2018-08-26 2019-05-10 熵零技术逻辑工程院集团股份有限公司 A kind of electrolysis unit
KR20220048590A (en) * 2020-10-13 2022-04-20 (주) 테크윈 A DEVICE FOR PRODUCING NaOH AND A DEVICE FOR PRODUCING NaOCl comprising the same
WO2022080793A1 (en) * 2020-10-13 2022-04-21 (주)테크윈 Apparatus for generating sodium hydroxide and apparatus for generating sodium hypochlorite comprising same
KR102433195B1 (en) * 2020-10-13 2022-08-19 (주)테크윈 A DEVICE FOR PRODUCING NaOH AND A DEVICE FOR PRODUCING NaOCl comprising the same
CN116770334A (en) * 2022-03-23 2023-09-19 李枭 Sodium hydroxide production system

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