JP2006137646A - Method for manufacturing low bromine inorganic salts - Google Patents
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Abstract
Description
本発明は低臭素無機塩類の製造方法に関する。 The present invention relates to a method for producing a low bromine inorganic salt.
近年、塩化ナトリウム、塩化カルシウムおよび塩化カリウム等に代表される数多くの無機塩類が食品および医薬品等の原料に用いられている。この分野で広く用いられている無機塩類の多くは海塩由来の物質である。このような無機塩類溶液は不純物として例えば臭化物塩を含むため、これら分野の商品全般においては前記臭化物塩を可能な限り除去することが望まれている。 In recent years, many inorganic salts represented by sodium chloride, calcium chloride, potassium chloride and the like have been used as raw materials for foods and pharmaceuticals. Many of the inorganic salts widely used in this field are substances derived from sea salt. Since such an inorganic salt solution contains, for example, a bromide salt as an impurity, it is desired to remove the bromide salt as much as possible in general products in these fields.
臭素除去技術として、一般的には、イオン交換膜法／電気分解法または活性炭やゼオライトを用いた吸着分離法が知られている。イオン交換膜法／電気分解法は、臭素除去に有効であるものの、塩化ナトリウムのような塩化物塩を対象にした場合、塩化物イオンと臭化物イオンの性質が類似するために臭化物イオンのみを選択的に除去することが困難である。吸着分離法は、吸着処理工程の設備費用およびランニングコスト等が高騰する問題がある。 As a bromine removal technique, an ion exchange membrane method / electrolysis method or an adsorption separation method using activated carbon or zeolite is generally known. The ion exchange membrane method / electrolysis method is effective for removing bromine. However, when chloride salts such as sodium chloride are used, only bromide ions are selected because the properties of chloride ions and bromide ions are similar. Is difficult to remove. The adsorptive separation method has a problem that the equipment cost and running cost of the adsorption treatment process increase.
特許文献１には、食塩水溶液に次亜塩素酸ナトリウムを添加して臭化物イオンを酸化させ、塩酸酸性に調整した後に、ガスでバブリングすることにより臭素として除去する方法が開示されている。
しかし、上述の特許文献１の方法によると、臭素ガスと共に多量の塩素ガスが発生する。塩素ガス自体、腐食性が高い上に人体にも極めて有害な物質であるため、安全性を考慮して、例えば塩素ガスを処理する排ガス処理設備が必要になる。また、臭素除去装置を耐食性の高い材料で製作する必要もある。その結果、前記設備を含めた装置が高コストになる問題がある。 However, according to the method of Patent Document 1 described above, a large amount of chlorine gas is generated together with bromine gas. Since chlorine gas itself is highly corrosive and extremely harmful to the human body, in consideration of safety, for example, an exhaust gas treatment facility for treating chlorine gas is required. It is also necessary to manufacture the bromine removal device with a material having high corrosion resistance. As a result, there is a problem that the apparatus including the equipment becomes expensive.
本発明は、上記の問題に鑑み、作業環境の悪化および過度な装置腐食を招くようなガスを系内に発生させることなく、臭素含有無機塩類から臭素を除去することが可能な低臭素無機塩類の製造方法を提供しようとするものである。 In view of the above problems, the present invention is a low bromine inorganic salt capable of removing bromine from a bromine-containing inorganic salt without generating in the system a gas that causes deterioration of the working environment and excessive equipment corrosion. It is intended to provide a manufacturing method.
本発明によると、臭化物イオン（Ｂｒ−）を含む無機塩類溶液に臭素酸イオン（ＢｒＯ３ −）および酸を添加して臭素を生成させる工程と、前記生成した臭素を気体として前記無機塩類溶液から放出させる工程とを含むことを特徴とする低臭素無機塩類の製造方法が提供される。 According to the present invention, bromine ions (BrO 3 − ) and an acid are added to an inorganic salt solution containing bromide ions (Br − ) to generate bromine, and the generated bromine is used as a gas from the inorganic salt solution. A process for producing the low bromine inorganic salts characterized in that it comprises a step of releasing.
本発明の無機塩類の製造において、前記臭素酸イオンは前記臭化物イオン１モルに対して、０．０５モルを超え、０．５モル未満の範囲で添加されることが好ましい。 In the production of the inorganic salts of the present invention, the bromate ion is preferably added in an amount exceeding 0.05 mol and less than 0.5 mol with respect to 1 mol of the bromide ion.
本発明の無機塩類の製造において、前記酸は、前記無機塩類溶液にｐＨが３以下になるように添加されることが好ましい。 In the production of the inorganic salts of the present invention, the acid is preferably added to the inorganic salt solution so that the pH is 3 or less.
本発明の無機塩類の製造において、前記生成した臭素を気体として放出する前記工程は、６０℃以上の温度の無機塩水溶液を用いることによりなされることを許容する。 In the production of the inorganic salts of the present invention, the step of releasing the produced bromine as a gas is allowed to be performed by using an inorganic salt aqueous solution having a temperature of 60 ° C. or higher.
本発明の無機塩類の製造において、前記生成した臭素を気体として放出する前記工程は、前記無機塩水溶液にガスをバブリングすることによりなされることを許容する。 In the production of the inorganic salts of the present invention, the step of releasing the produced bromine as a gas is allowed to be performed by bubbling gas into the inorganic salt aqueous solution.
また本発明によると、臭化物イオン（Ｂｒ−）を含む６０℃以上の無機塩類溶液に臭素酸イオン（ＢｒＯ３ −）および酸を添加して臭素を生成させた後、その温度を所望時間保持させることにより前記生成した臭素を気体として前記無機塩類溶液から放出させることを特徴とする低臭素無機塩類の製造方法が提供される。 According to the present invention, bromate ions (BrO 3 − ) and an acid are added to an inorganic salt solution containing bromide ions (Br − ) at 60 ° C. or higher to form bromine, and then the temperature is maintained for a desired time. Accordingly, a method for producing a low bromine inorganic salt is provided, wherein the produced bromine is released as a gas from the inorganic salt solution.
本発明によれば、比較的低コストの装置で臭素含有量が低減された低臭素無機塩類の製造方法を提供することができる。 ADVANTAGE OF THE INVENTION According to this invention, the manufacturing method of the low bromine inorganic salt by which bromine content was reduced with the apparatus of comparatively low cost can be provided.
以下本発明に係る低臭素無機塩類の製造方法を説明する。 The method for producing the low bromine inorganic salts according to the present invention will be described below.
まず、臭化物イオンを含有する無機塩類溶液、例えば無機塩類水溶液に臭素酸イオンおよび酸を添加することにより臭素を生成させる。 First, bromine is generated by adding bromate ions and an acid to an inorganic salt solution containing bromide ions, for example, an aqueous inorganic salt solution.
前記無機塩としては例えば塩化ナトリウム、塩化カリウムおよび塩化マグネシウムなどの塩化物塩、硫酸塩または硝酸塩等を挙げることができる。 Examples of the inorganic salt include chloride salts such as sodium chloride, potassium chloride and magnesium chloride, sulfates and nitrates.
臭素は臭化物イオン（Ｂｒ−）として、例えば臭化ナトリウム、臭化カリウム、臭化マグネシウム等の臭化物塩の形態で前記無機塩類溶液に含まれる。 Bromine is contained in the inorganic salt solution as bromide ions (Br − ) in the form of bromide salts such as sodium bromide, potassium bromide and magnesium bromide.
前記臭素酸イオン（ＢｒＯ３ −）は、例えば臭素酸ナトリウム、臭素酸カリウム、臭素酸マグネシウムの形態で前記無機塩類溶液に添加される。 The bromate ion (BrO 3 − ) is added to the inorganic salt solution in the form of, for example, sodium bromate, potassium bromate, or magnesium bromate.
前記臭素酸イオンの添加量は、前記臭素含有無機塩類溶液中に含まれる臭化物イオン１モルに対して０．０５モルを超え０．５モル未満の範囲にすることが好ましい。臭素酸イオンの添加量を臭化物イオン１モルに対して０．０５モル以下にすると、無機塩類溶液中の臭化物イオンを十分に除去することが困難になる。一方、臭素酸イオンの添加量を臭化物イオン１モルに対し０．５モル以上にすると、無機塩類溶液中に残留する臭素酸イオン量が多くなる恐れがある。より好ましい前記臭素酸イオンの添加量は、臭化物イオン１モルに対し、０．１モルを超え０．３モル未満の範囲である。 The amount of bromate ion added is preferably more than 0.05 mol and less than 0.5 mol with respect to 1 mol of bromide ion contained in the bromine-containing inorganic salt solution. When the amount of bromate ion added is 0.05 mol or less with respect to 1 mol of bromide ion, it is difficult to sufficiently remove bromide ion in the inorganic salt solution. On the other hand, when the amount of bromate ion added is 0.5 mol or more with respect to 1 mol of bromide ion, the amount of bromate ion remaining in the inorganic salt solution may increase. The more preferable addition amount of the bromate ion is in the range of more than 0.1 mol and less than 0.3 mol per mol of bromide ion.
前記無機塩類溶液への酸の添加にあたって、ｐＨ３以下に調節し、溶液中に含まれる臭化物イオンを臭素に変換する反応を促進することが好ましい。より好ましい酸添加によるｐＨは２以下である。前記酸としては、例えば塩酸、硫酸および硝酸等が挙げられる。 In addition of the acid to the inorganic salt solution, it is preferable to adjust the pH to 3 or less to promote the reaction of converting bromide ions contained in the solution into bromine. The pH by the more preferable acid addition is 2 or less. Examples of the acid include hydrochloric acid, sulfuric acid, and nitric acid.
前記臭素生成において、臭化ナトリウム（ＮａＢｒ）を含む塩化ナトリウム水溶液に臭素酸ナトリウム（ＮａＢｒＯ３）および硫酸（Ｈ２ＳＯ４）を添加して処理する場合、下記式（１）の反応により水溶液中に臭素が生成する。 In the bromine production, when sodium bromate (NaBrO 3 ) and sulfuric acid (H 2 SO 4 ) are added to a sodium chloride aqueous solution containing sodium bromide (NaBr) for treatment, the reaction is performed in the aqueous solution by the reaction of the following formula (1). Bromine is formed.
５ＮａＢｒ + ＮａＢｒＯ３ + ３Ｈ２ＳＯ４ →
３Ｂｒ２ + ３Ｎａ２ＳＯ４ + ３Ｈ２Ｏ …（１）
また、臭化カリウム（ＫＢｒ）を含む塩化カリウム水溶液に臭素酸カリウム（ＮａＢｒＯ３）および塩酸（ＨＣｌ）を添加して処理する場合、下記式（２）の反応により水溶液中に臭素が生成する。
5NaBr + NaBrO 3 + 3H 2 SO 4 →
3Br 2 + 3Na 2 SO 4 + 3H 2 O ... (1)
Further, when potassium bromate (NaBrO 3 ) and hydrochloric acid (HCl) are added to a potassium chloride aqueous solution containing potassium bromide (KBr) for treatment, bromine is generated in the aqueous solution by the reaction of the following formula (2).
５ＫＢｒ + ＫＢｒＯ３ + ６ＨＣｌ → ３Ｂｒ２ + ６ＫＣｌ + ３Ｈ２Ｏ …（２）
前記各式に示すように、前記水溶液中の臭化物イオン１モルに対する臭素酸イオンの反応当量は０．２モルである。
5KBr + KBrO 3 + 6HCl → 3Br 2 + 6KCl + 3H 2 O (2)
As shown in the above formulas, the reaction equivalent of bromate ion to 1 mol of bromide ion in the aqueous solution is 0.2 mol.
前記臭素酸イオンの塩、およびｐＨ調整のための酸添加にあたって、臭素を生成するための反応系で随伴する塩が製造対象である無機塩類と同じ物質になるようにそれらを選択すれば、生成される塩が前記無機塩類に異物質として含有されるのを回避できる。具体的には、製造対象の無機塩類が塩化カリウムである場合、臭素酸イオンの塩として臭素酸カリウム、酸として塩酸を選択すれば前述した式（２）の反応から臭素の生成と共に、製造対象と同じ塩化カリウムを生成することが可能になる。 When the salt of bromate ion and the acid added for pH adjustment are selected so that the accompanying salt in the reaction system for producing bromine is the same substance as the inorganic salt to be produced, It is possible to avoid the salt to be contained as a foreign substance in the inorganic salt. Specifically, when the inorganic salt to be produced is potassium chloride, if potassium bromate is selected as the bromate ion salt and hydrochloric acid is selected as the acid, bromine is produced from the reaction of formula (2) described above and the production object The same potassium chloride can be produced.
次いで、前述した処理により無機塩類中に生成させた臭素をガスとして放出除去する。 Next, bromine produced in the inorganic salt by the above-described treatment is released and removed as a gas.
前記臭素の放出除去手段の１つとして、加熱処理方法を採用することができる。臭素は常圧下で６０℃の沸点を有することから、臭素生成後の無機塩類溶液を６０℃以上に加熱することによりその臭素をガスとして放出除去する。 As one of the means for removing and removing bromine, a heat treatment method can be adopted. Since bromine has a boiling point of 60 ° C. under normal pressure, the bromine is released and removed as a gas by heating the inorganic salt solution after bromine generation to 60 ° C. or higher.
前記放出除去手段の他の手段として、空気または不活性ガス等のガスを臭素生成後の無機塩類溶液にバブリングする方法を採用することができる。前記不活性ガスとしては例えば窒素等を挙げることができる。なお、このバブリングにおいて、臭素が生成された無機塩類溶液を６０℃以上に加熱してもよい。 As another means for the release and removal means, a method of bubbling a gas such as air or an inert gas into the inorganic salt solution after bromine production can be employed. Examples of the inert gas include nitrogen. In this bubbling, the inorganic salt solution in which bromine is generated may be heated to 60 ° C. or higher.
前述した方法で放出、除去した臭素は、スクラバーを用いて水に接触させるか、またはアルカリ溶液中に通すか、いずれかにより容易に回収できる。 The bromine released and removed by the above-described method can be easily recovered by either contacting with water using a scrubber or passing through an alkaline solution.
次いで、臭素を除去した無機塩類溶液から低臭素無機塩類を製造する。具体的には、水に対する溶解度が高い温度依存性を示す無機塩類の場合には溶解度差を利用して結晶を析出する方法を採用する。すなわち、臭素除去後、無機塩類溶液をその塩類が十分に溶解し得る６０℃以上に加熱し、その後冷却して無機塩類の結晶を析出させる。続いて、結晶が析出した溶液を固液分離し、乾燥することにより、無機塩類結晶、つまり低臭素無機塩類を製造する。 Next, a low bromine inorganic salt is produced from the inorganic salt solution from which bromine has been removed. Specifically, in the case of inorganic salts that have high water solubility and temperature dependency, a method of precipitating crystals using the solubility difference is employed. That is, after removing bromine, the inorganic salt solution is heated to 60 ° C. or higher at which the salt can be sufficiently dissolved, and then cooled to precipitate inorganic salt crystals. Subsequently, the solution in which the crystals are precipitated is solid-liquid separated and dried to produce inorganic salt crystals, that is, low bromine inorganic salts.
ただし、前述した実施形態では無機塩類の溶液状態でいくつかの処理を施すことから、臭素酸イオンの添加時の無機塩類水溶液の温度を６０℃以上とし、臭素の生成、除去の工程中にこの温度を保持することにより、その後の冷却により無機塩類の結晶を析出させることが可能である。また、このような温度保持は前述した臭素をガスとして放出、除去する工程も兼用させることが可能で、工程数の短縮（省略）にも寄与することができる。 However, in the above-described embodiment, since some treatment is performed in a solution state of inorganic salts, the temperature of the inorganic salt aqueous solution at the time of adding bromate ions is set to 60 ° C. or more, and this process is performed during the bromine generation and removal process. By maintaining the temperature, it is possible to precipitate inorganic salt crystals by subsequent cooling. Further, such temperature holding can also be used for the above-described process of releasing and removing bromine as a gas, and can contribute to shortening (omitting) the number of processes.
なお、前記臭素を除去した無機塩類溶液から低臭素無機塩類を製造する方法は、前述した溶解度差を利用する再結晶法に限られず、蒸発乾固、減圧蒸留、中和反応による晶析方法等のような他の晶析方法を採用してもよい。 The method for producing low bromine inorganic salts from the inorganic salt solution from which bromine has been removed is not limited to the recrystallization method using the above-described solubility difference, evaporating to dryness, vacuum distillation, crystallization method by neutralization reaction, etc. Other crystallization methods such as
以上説明したように、本発明の実施形態によれば臭素を含有する無機塩類溶液に臭素酸イオンを添加することにより、従来のように腐食性の高い塩素ガスを随併することなく臭素を生成できる。この後、生成した臭素をガスとして放出、除去することにより、低臭素濃度の無機塩類溶液が得られ、これから低臭素無機塩類を製造できる。 As described above, according to the embodiment of the present invention, bromine is generated without adding a highly corrosive chlorine gas as in the prior art by adding bromate ions to an inorganic salt solution containing bromine. it can. Thereafter, the produced bromine is released and removed as a gas to obtain an inorganic salt solution having a low bromine concentration, from which a low bromine inorganic salt can be produced.
したがって、作業環境の悪化、および装置の腐食を招く塩素ガスを系内に発生させることなく、比較的低コストの装置を用いて低臭素無機塩類を製造できる。 Therefore, low bromine inorganic salts can be produced by using a relatively low cost apparatus without generating chlorine gas in the system which causes deterioration of the working environment and corrosion of the apparatus.
特に、臭素酸イオンの添加量、酸添加によるｐＨ値および臭素生成後の無機塩類溶液の６０℃以上の温度保持および／または同溶液へのガスのバブリングのいずれかを規定することによって、より低臭素の無機塩類を製造できる。また、これらの条件を全て規定することにより、例えば臭素含有量が５０ｍｇ／ｋｇ以下の低臭素無機塩類を製造することが可能になる。 In particular, by specifying either the amount of bromate ion added, the pH value due to acid addition and the temperature of the inorganic salt solution after bromine formation at 60 ° C. or higher and / or the bubbling of gas into the solution. Inorganic salts of bromine can be produced. Further, by prescribing all these conditions, it is possible to produce low bromine inorganic salts having a bromine content of 50 mg / kg or less, for example.
以下、実施例を示して本発明についてさらに詳細に説明する。 Hereinafter, the present invention will be described in more detail with reference to examples.
（比較例１）
塩化カリウム（（株）富田製薬製）４０重量％溶液（溶液温度８０℃）に、臭化カリウム（和光純薬製）を加えて臭化物イオン濃度１０００ｍｇ／Ｌの溶液を調製し、これを溶液Ａとした。溶液Ａの温度を８０℃に２時間保持させた後、溶液の一部をサンプリングした。その後、直ちに容器外部を水道水に浸漬／通水させ冷却して、最終溶液温度を３０℃にし、塩化カリウムの結晶を析出させた。晶析後、固液分離／乾燥を行い、塩化カリウムの結晶を製造した。
(Comparative Example 1)
Potassium bromide (manufactured by Tomita Pharmaceutical Co., Ltd.) 40 wt% solution (solution temperature 80 ° C.) is added with potassium bromide (manufactured by Wako Pure Chemical Industries) to prepare a solution having a bromide ion concentration of 1000 mg / L. It was. After keeping the temperature of the solution A at 80 ° C. for 2 hours, a part of the solution was sampled. Thereafter, the outside of the container was immediately immersed / passed in tap water and cooled to bring the final solution temperature to 30 ° C. to precipitate potassium chloride crystals. After crystallization, solid-liquid separation / drying was performed to produce potassium chloride crystals.
（実施例１）
比較例１と同様な溶液Ａ（臭化物イオン濃度１０００ｍｇ／Ｌ）にＫＢｒＯ３を臭素酸イオン濃度で８０ｍｇ／Ｌになるように加え、溶液中の臭化物イオン１モルに対する臭素酸イオンを０．０５モルに調整して、溶液Ｂとした。なお、臭化物イオン１モルに対する臭素酸イオンのモル数を以下に単にモル比と称する。この溶液Ｂに塩酸（３５％、和光純薬製）を加えて溶液をｐＨ１．５に調整した。この溶液の温度を８０℃に２時間保持させた後、その一部をサンプリングした。その後、直ちに容器外部を水道水に浸漬／通水させ冷却して、最終溶液温度を３０℃にし、塩化カリウムの結晶を析出させた。晶析後、固液分離／乾燥を行い、塩化カリウムの結晶を製造した。
Example 1
KBrO 3 was added to the same solution A (bromide ion concentration 1000 mg / L) as in Comparative Example 1 so that the bromate ion concentration was 80 mg / L, and 0.05 mol of bromate ion relative to 1 mol of bromide ion in the solution was added. To prepare Solution B. In addition, the number of moles of bromate ion with respect to 1 mole of bromide ions is hereinafter simply referred to as a molar ratio. To this solution B, hydrochloric acid (35%, manufactured by Wako Pure Chemical Industries) was added to adjust the solution to pH 1.5. After maintaining the temperature of this solution at 80 ° C. for 2 hours, a part thereof was sampled. Thereafter, the outside of the container was immediately immersed / passed in tap water and cooled to bring the final solution temperature to 30 ° C. to precipitate potassium chloride crystals. After crystallization, solid-liquid separation / drying was performed to produce potassium chloride crystals.
（実施例２）
実施例１と同様な溶液Ｂ（モル比；０．０５）に塩酸を加えて溶液をｐＨ３．５に調整した以外、実施例１と同様の方法でサンプリングし、かつ塩化カリウムの結晶を製造した。
(Example 2)
Sampling was carried out in the same manner as in Example 1 except that hydrochloric acid was added to the same solution B (molar ratio; 0.05) as in Example 1 to adjust the solution to pH 3.5, and potassium chloride crystals were produced. .
（実施例３）
比較例１と同様な溶液Ａ（臭化物イオン濃度１０００ｍｇ／Ｌ）にＫＢｒＯ３を臭素酸イオン濃度で１６０ｍｇ／Ｌになるように加え、溶液中のモル比を０．１に調整して、溶液Ｃとした。この溶液Ｃに塩酸（３５％、和光純薬製）を加えて溶液をｐＨ１．５に調整した。この溶液の温度を８０℃に２時間保持させた後、その一部をサンプリングした。その後、直ちに容器外部を水道水に浸漬／通水させ冷却して、最終溶液温度を３０℃にし、塩化カリウムの結晶を析出させた。晶析後、固液分離／乾燥を行い、塩化カリウムの結晶を製造した。
(Example 3)
KBrO 3 was added to the same solution A (bromide ion concentration 1000 mg / L) as in Comparative Example 1 so that the bromate ion concentration was 160 mg / L, and the molar ratio in the solution was adjusted to 0.1, so that the solution C It was. To this solution C, hydrochloric acid (35%, manufactured by Wako Pure Chemical Industries, Ltd.) was added to adjust the solution to pH 1.5. After maintaining the temperature of this solution at 80 ° C. for 2 hours, a part thereof was sampled. Thereafter, the outside of the container was immediately immersed / passed in tap water and cooled to bring the final solution temperature to 30 ° C. to precipitate potassium chloride crystals. After crystallization, solid-liquid separation / drying was performed to produce potassium chloride crystals.
（実施例４）
実施例３と同様な溶液Ｃ（モル比；０．１）に塩酸を加えて溶液をｐＨ３．５に調整した以外、実施例３と同様の方法でサンプリングし、かつ塩化カリウムの結晶を製造した。
Example 4
Sampling was carried out in the same manner as in Example 3 except that hydrochloric acid was added to the same solution C (molar ratio; 0.1) as in Example 3 to adjust the solution to pH 3.5, and potassium chloride crystals were produced. .
（実施例５）
比較例１と同様な溶液Ａ（臭化物イオン濃度１０００ｍｇ／Ｌ）にＫＢｒＯ３を臭素酸イオン濃度で３２０ｍｇ／Ｌになるように加え、溶液中のモル比を０．２に調整して、溶液Ｄとした。この溶液Ｄに塩酸（３５％、和光純薬製）を加えて溶液をｐＨ１．５に調整し、溶液Ｅとした。この溶液Ｅの調製直後にサンプリングした。その後、直ちに容器外部を水道水に浸漬／通水させ冷却して、最終溶液温度を３０℃にし、塩化カリウムの結晶を析出させた。晶析後、固液分離／乾燥を行い、塩化カリウムの結晶を製造した。
(Example 5)
KBrO 3 was added to the same solution A as in Comparative Example 1 (bromide ion concentration 1000 mg / L) so that the bromate ion concentration was 320 mg / L, and the molar ratio in the solution was adjusted to 0.2, so that Solution D It was. To this solution D, hydrochloric acid (35%, manufactured by Wako Pure Chemical Industries, Ltd.) was added to adjust the solution to pH 1.5 to obtain a solution E. The solution E was sampled immediately after preparation. Thereafter, the outside of the container was immediately immersed / passed in tap water and cooled to bring the final solution temperature to 30 ° C. to precipitate potassium chloride crystals. After crystallization, solid-liquid separation / drying was performed to produce potassium chloride crystals.
（実施例６）
実施例５と同様な溶液Ｅ（モル比；０．２、ｐＨ１．５）の調製後に、８０℃に２時間保持させ、かつ保持後に溶液の一部をサンプリングした以外、実施例５と同様の方法で塩化カリウムの結晶を製造した。
(Example 6)
After preparing the same solution E (molar ratio; 0.2, pH 1.5) as in Example 5, it was held at 80 ° C. for 2 hours, and after holding, a part of the solution was sampled, and the same as in Example 5 According to this method, crystals of potassium chloride were produced.
（実施例７）
実施例５と同様な溶液Ｄ（モル比；０．２）に塩酸（３５％、和光純薬製）を加えて溶液をｐＨ２．５に調整し、溶液Ｆとした。この溶液の温度を８０℃に２時間保持させた後、その一部をサンプリングした。その後、直ちに容器外部を水道水に浸漬／通水させ冷却して、最終溶液温度を３０℃にし、塩化カリウムの結晶を析出させた。晶析後、固液分離／乾燥を行い、塩化カリウムの結晶を製造した。
(Example 7)
Hydrochloric acid (35%, manufactured by Wako Pure Chemical Industries, Ltd.) was added to the same solution D (molar ratio; 0.2) as in Example 5 to adjust the solution to pH 2.5. After maintaining the temperature of this solution at 80 ° C. for 2 hours, a part thereof was sampled. Thereafter, the outside of the container was immediately immersed / passed in tap water and cooled to bring the final solution temperature to 30 ° C. to precipitate potassium chloride crystals. After crystallization, solid-liquid separation / drying was performed to produce potassium chloride crystals.
（実施例８）
実施例５と同様な溶液Ｄ（モル比；０．２）に塩酸（３５％、和光純薬製）を加えて溶液をｐＨ１．５に調整し溶液Ｇとした。溶液Ｇの調製直後その一部をサンプリングした。その後、直ちに容器外部を水道水に浸漬／通水させ冷却して、最終溶液温度を３０℃にし、塩化カリウムの結晶を析出させた。晶析後、固液分離／乾燥を行い、塩化カリウムの結晶を製造した。
(Example 8)
Hydrochloric acid (35%, manufactured by Wako Pure Chemical Industries, Ltd.) was added to the same solution D (molar ratio; 0.2) as in Example 5 to adjust the solution to pH 1.5 to obtain a solution G. A portion of the solution G was sampled immediately after preparation. Thereafter, the outside of the container was immediately immersed / passed in tap water and cooled to bring the final solution temperature to 30 ° C. to precipitate potassium chloride crystals. After crystallization, solid-liquid separation / drying was performed to produce potassium chloride crystals.
（実施例９）
実施例８と同様な溶液Ｇ（モル比；０．２、ｐＨ３．５）の調製後に８０℃に２時間保持させ、かつ保持後に溶液の一部をサンプリングした以外、実施例８と同様の方法で塩化カリウムの結晶を製造した。
Example 9
The same method as in Example 8 except that the preparation of the solution G (molar ratio; 0.2, pH 3.5) similar to that in Example 8 was maintained at 80 ° C. for 2 hours and a part of the solution was sampled after the holding. Produced potassium chloride crystals.
上記比較例および実施例１〜９においてサンプリングした溶液の臭化物イオン濃度を測定した。また、各例で製造した塩化カリウムの結晶の一部をそれぞれ水に溶解させ臭化物イオン濃度を測定した。なお溶液中および結晶中の臭化物イオン濃度の測定は、European Phamacoeia 1997の第３版（１９９９年改訂）、P.1198の塩化カリウムに含まれる臭化物の検出方法に準じた方法を用いて行った。装置は分光光度計（（株）日立製作所、型式：Ｕ−３２１０、波長５９０ｎｍ、光路長１０ｍｍ）を用いた。これらの測定の結果を下記の表１に示す。
前記表１から明らかなように、臭化カリウムを含む塩化カリウムの水溶液に臭素酸カリウムを添加した実施例１〜９は臭素酸カリウム無添加の比較例１に比べて塩化カリウム水溶液中の臭化物イオン濃度を低減でき、かつ塩化カリウムの結晶中の臭素含有量も低減できることがわかる。 As is apparent from Table 1, Examples 1 to 9 in which potassium bromate was added to an aqueous solution of potassium chloride containing potassium bromide were compared with Comparative Example 1 in which potassium bromate was not added. It can be seen that the concentration can be reduced and the bromine content in the potassium chloride crystals can also be reduced.
特に、ｐＨおよび８０℃の保持時間が同じ条件で臭素酸カリウムのモル比が異なる実施例１、３、６群（または実施例２、９群）を対比すると、臭素酸カリウムのモル比が０．０５モルを超え、０．５モル未満の実施例３，６（または実施例９）は、モル比が前記範囲外の実施例１（または実施例２）に比べて塩化カリウム水溶液中の臭化物イオン濃度をより低減でき、かつ塩化カリウムの結晶中の臭素含有量もより低減できることがわかる。 In particular, when Examples 1, 3, and 6 groups (or Examples 2 and 9 groups) having different pH ratios and different molar ratios of potassium bromate under the same conditions are compared, the molar ratio of potassium bromate is 0. Examples 3 and 6 (or Example 9) having a molar ratio of more than 0.05 mol and less than 0.5 mol are compared with Example 1 (or Example 2) in which the molar ratio is outside the above range, bromide in an aqueous potassium chloride solution. It can be seen that the ion concentration can be further reduced and the bromine content in the potassium chloride crystals can be further reduced.
また、臭素酸カリウムのモル比および８０℃の保持時間が同じ条件でｐＨが異なる実施例１，２群（または実施例３，４群、さらに実施例６、７，９群）を対比すると、ｐＨが３以下の実施例１（または実施例３、さらに実施例６，７）はｐＨが３を超える実施例２（または実施例４、さらに実施例９）に比べて塩化カリウム水溶液中の臭化物イオン濃度をより低減でき、かつ塩化カリウムの結晶中の臭素含有量もより低減できることがわかる。 Further, when comparing the molar ratio of potassium bromate and Examples 1 and 2 groups (or Examples 3 and 4 groups, and further Examples 6 and 7 and 9 groups) having different pHs under the same conditions for the retention time of 80 ° C, Example 1 (or Example 3, and Examples 6 and 7) having a pH of 3 or less is bromide in an aqueous potassium chloride solution compared to Example 2 (or Example 4 and Example 9) having a pH of more than 3. It can be seen that the ion concentration can be further reduced and the bromine content in the potassium chloride crystals can be further reduced.
さらに、臭素酸カリウムのモル比およびｐＨが同じ条件で８０℃の保持工程の有無［実施例５，６群（または実施例８，９群）］を対比すると、８０℃の保持工程を有する実施例６（または実施例９）は保持工程のない実施例５（または実施例８）に比べて臭素含有量の低減効果が高いことがわかる。 Furthermore, when the molar ratio of potassium bromate and the pH are the same, the presence or absence of a holding step at 80 ° C. [Examples 5 and 6 (or Examples 8 and 9)] is compared. It can be seen that Example 6 (or Example 9) has a higher bromine content reducing effect than Example 5 (or Example 8) without the holding step.
中でも、臭素酸カリウムのモル比が０．０５モルを超え、０．５モル未満で、ｐＨが３以下、８０℃の保持工程を有する実施例３，４，６，７は塩化カリウム水溶液中の臭化物イオン濃度をより一層低減でき、かつ塩化カリウムの結晶中の臭素含有量もより一層低減できることがわかる。 Among them, Examples 3, 4, 6, and 7 having a holding step of a potassium bromate molar ratio of more than 0.05 mol, less than 0.5 mol, pH of 3 or less, and 80 ° C. It can be seen that the bromide ion concentration can be further reduced and the bromine content in the potassium chloride crystals can be further reduced.
（実施例１０）
実施例３と同様な溶液Ｃ（モル比；０．２）に塩酸（３５％、和光純薬製：）を加えてｐＨ１．５の溶液を調整した。この溶液に空気を１時間あたり１００Ｌの流量で２時間バブリングした。バブリング直後にその溶液の一部をサンプリングした。その後、直ちに容器外部を水道水に浸漬／通水させ冷却して、最終溶液温度を３０℃にし、塩化カリウムの結晶を析出させた。晶析後、固液分離／乾燥を行い、塩化カリウムの結晶を製造した。
(Example 10)
Hydrochloric acid (35%, manufactured by Wako Pure Chemical Industries, Ltd.) was added to the same solution C (molar ratio; 0.2) as in Example 3 to prepare a pH 1.5 solution. Air was bubbled through this solution for 2 hours at a flow rate of 100 L per hour. A portion of the solution was sampled immediately after bubbling. Thereafter, the outside of the container was immediately immersed / passed in tap water and cooled to bring the final solution temperature to 30 ° C. to precipitate potassium chloride crystals. After crystallization, solid-liquid separation / drying was performed to produce potassium chloride crystals.
（実施例１１）
実施例５と同様な溶液Ｅ（モル比；０．２、ｐＨ１．５）に空気を１時間あたり１００Ｌの流量で２時間バブリングした。バブリング直後にその溶液の一部をサンプリングした。その後、直ちに容器外部を水道水に浸漬／通水させ冷却して、最終溶液温度を３０℃にし、塩化カリウムの結晶を析出させた。晶析後、固液分離／乾燥を行い、塩化カリウムの結晶を製造した。
(Example 11)
Air was bubbled into solution E (molar ratio; 0.2, pH 1.5) similar to Example 5 at a flow rate of 100 L per hour for 2 hours. A portion of the solution was sampled immediately after bubbling. Thereafter, the outside of the container was immediately immersed / passed in tap water and cooled to bring the final solution temperature to 30 ° C. to precipitate potassium chloride crystals. After crystallization, solid-liquid separation / drying was performed to produce potassium chloride crystals.
上記実施例１０、１１においてサンプリングした溶液の臭化物イオン濃度を前述した方法で測定した。また、各例で製造した塩化カリウムの結晶の一部をそれぞれ水に溶解させ臭化物イオン濃度を前述した方法で測定した。これらの測定を下記表２に示す。なお、下記表２には参考としての実施例３および６を併記する。
前記表２から明らかなように、臭化カリウムを含む塩化カリウムの水溶液に臭素酸カリウムを添加し、バブリングする実施例１０および１１は臭素酸カリウム無添加の比較例１に比べて塩化カリウム水溶液中の臭化物イオン濃度を低減でき、かつ塩化カリウムの結晶中の臭素含有量も低減できることがわかる。 As apparent from Table 2, Examples 10 and 11 in which potassium bromate was added to an aqueous solution of potassium chloride containing potassium bromide and bubbled were compared with Comparative Example 1 in which potassium bromate was not added. It can be seen that the bromide ion concentration can be reduced and the bromine content in the potassium chloride crystals can also be reduced.
特に、臭素酸カリウムのモル比、ｐＨが同じ条件で、生成した臭素除去手段のみが異なる実施例３、１０群（または実施例６、１１群）を対比すると、臭素除去手段がバブリングである実施例１０（または実施例１１）は同手段が８０℃保持である実施例３（または６）と同様な優れた臭素低減効果を示した。 In particular, when Examples 3 and 10 groups (or Examples 6 and 11 groups) differing only in the bromine removal means produced under the same potassium bromate molar ratio and pH conditions, the bromine removal means is bubbling. Example 10 (or Example 11) showed an excellent bromine reducing effect similar to Example 3 (or 6) in which the same means was maintained at 80 ° C.
本発明による前述の実施例に従うことで、臭素含有の無機塩類の臭素含有量を低減させ、低臭素含有の無機塩類を製造することが可能になる。特に実施例６のように、無機塩類水溶液のｐＨを２以下にし、臭素酸イオン／臭化物イオンのモル比が０．２／１となるように臭素酸イオンを添加し、かつ溶液を十分な時間６０℃以上に保持することにより、５０ｍｇ／ｋｇ以下という極めて低い臭素含有量の無機塩類を製造することができる。 By following the above-described embodiments according to the present invention, it is possible to reduce the bromine content of bromine-containing inorganic salts and to produce low bromine-containing inorganic salts. In particular, as in Example 6, the pH of the inorganic salt aqueous solution was set to 2 or less, bromate ions were added so that the bromate ion / bromide ion molar ratio was 0.2 / 1, and the solution was allowed to have sufficient time. By maintaining the temperature at 60 ° C. or higher, inorganic salts having an extremely low bromine content of 50 mg / kg or less can be produced.
なお、実施例では無機塩類として、臭化カリウムを含有する塩化カリウムを用いたが、塩化ナトリウムのような他の種類の無機塩類中の臭化物の含有量を同様な方法で低減させることが可能である。 In the examples, potassium chloride containing potassium bromide was used as the inorganic salt. However, the bromide content in other types of inorganic salts such as sodium chloride can be reduced in the same manner. is there.
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