JPH0867667A - Aqueous solution containing perdicarboxylic acid - Google Patents

Aqueous solution containing perdicarboxylic acid

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Publication number
JPH0867667A
JPH0867667A JP7144136A JP14413695A JPH0867667A JP H0867667 A JPH0867667 A JP H0867667A JP 7144136 A JP7144136 A JP 7144136A JP 14413695 A JP14413695 A JP 14413695A JP H0867667 A JPH0867667 A JP H0867667A
Authority
JP
Japan
Prior art keywords
acid
solution
mol
perdicarboxylic
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.)
Granted
Application number
JP7144136A
Other languages
Japanese (ja)
Other versions
JP3537540B2 (en
Inventor
Ritsuo Abe
律雄 阿部
Shinpei Hashimoto
新平 橋本
Hideko Ohashi
英子 大橋
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.)
Nippon Peroxide Co Ltd
Original Assignee
Nippon Peroxide Co Ltd
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 Nippon Peroxide Co Ltd filed Critical Nippon Peroxide Co Ltd
Priority to JP14413695A priority Critical patent/JP3537540B2/en
Publication of JPH0867667A publication Critical patent/JPH0867667A/en
Application granted granted Critical
Publication of JP3537540B2 publication Critical patent/JP3537540B2/en
Anticipated expiration legal-status Critical
Expired - Fee Related legal-status Critical Current

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  • Organic Low-Molecular-Weight Compounds And Preparation Thereof (AREA)
  • Agricultural Chemicals And Associated Chemicals (AREA)

Abstract

PURPOSE: To obtain an aqueous solution containing a perdicarboxylic acid, capable of efficiently forming a peracid by using a combined dicarboxylic acid and better in stability, performance or economical efficiency than those in the case of using a single carboxylic acid and useful for sterilizing, bleaching or cleaning. CONSTITUTION: The aqueous solution containing a perdicarboxylic acid is obtained by reacting a combined dicarboxylic acid containing glutaric acid and succinic acid with hydrogen peroxide and contains (1) 0.05-1.0mol/kg solution (expressed in terms of monoperdicarboxylic acid) perdicarboxylic acid, (2) 0.2-2.2 mol/kg solution total dicarboxylic acids except the perdicarboxlic acid, (3) 1.0-12.0mol/kg solution hydrogen peroxide and (4) a stabilizer at 0.01-3.0wt.% concentration and the succinic acid (including persuccinic acid) at a concentration within the range of 0.1-0.7mol/kg solution succinic acid at 0.1-2.0 molar ratio of the succinic acid (including persuccinic acid) to 1mol glutaric acid (including perglutaric acid).

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、殺菌、漂白、洗浄等の
用途に使用される安定な過ジカルボン酸含有水溶液組成
物、及びその製法に関する。
BACKGROUND OF THE INVENTION 1. Field of the Invention The present invention relates to a stable perdicarboxylic acid-containing aqueous composition used for applications such as sterilization, bleaching and washing, and a method for producing the same.

【0002】[0002]

【従来の技術】過カルボン酸類は、通常、カルボン酸或
いはカルボン酸無水物と過酸化水素から合成され、その
酸化力から種々物質の酸化剤として広く利用されると共
に、良好な殺菌、漂白、洗浄等の作用を示すことからこ
れらの用途にも使用されている。 これら過酸類の利用
形態としては固形のものと水溶液状のものとに大別され
るが、水溶液状の過カルボン酸としては過酢酸がその代
表的なものとして知られている。過酢酸はその安定性、
或いは原料となる酢酸の一般性から殺菌、漂白、洗浄等
の用途に汎用されているが、用途によっては過酢酸の有
する特有の臭いによってその使用が制約される場合があ
り、この問題を解決するために種々の安定かつ無臭性の
過酸類が検討され、特開昭53-81619 では無臭性の安定
な過グルタル酸濃厚液が提案されている。
BACKGROUND OF THE INVENTION Percarboxylic acids are usually synthesized from carboxylic acids or carboxylic acid anhydrides and hydrogen peroxide, and are widely used as oxidants for various substances due to their oxidizing power, as well as good sterilization, bleaching and washing. It is also used in these applications because it exhibits such effects. The usage forms of these peracids are roughly classified into solid ones and aqueous ones, and peracetic acid is known as a typical one of the aqueous percarboxylic acids. Peracetic acid is its stability,
Alternatively, it is widely used for applications such as sterilization, bleaching and washing due to the generality of acetic acid as a raw material, but depending on the application, its use may be restricted by the peculiar odor of peracetic acid, which solves this problem. Therefore, various stable and odorless peracids have been studied, and Japanese Patent Laid-Open No. 53-81619 proposes a stable odorless perglutaric acid concentrate.

【0003】無臭性の過酸類としては他に、過コハク
酸、過アジピン酸等の過ジカルボン酸類が挙げられる
が、過酸の生成は原料となるカルボン酸および過酸化水
素と、生成する過酸との平衡反応であるため、反応時の
カルボン酸、過酸化水素はそれらの濃度が高いほど効率
的に過酸が生成するのに対し、これら過酸の原料となる
コハク酸、アジピン酸の水溶解性は低く、効率的な過酸
の形成が行われないため、製造効率の点で不利であり、
また、低い濃度の過酸溶液しか得ることが出来ないた
め、流通上に於いても不利であるなどの理由から、これ
らの過酸の生成には専ら無水コハク酸あるいは無水アジ
ピン酸等の酸無水物が原料として使用されている。
Other odorless peracids include perdicarboxylic acids such as persuccinic acid and peradipic acid. The peracid is produced by using the carboxylic acid and hydrogen peroxide as raw materials and the peracid produced. Since carboxylic acid and hydrogen peroxide during the reaction are more equilibrium with peroxidic acid, the higher the concentration of them, the more efficiently the peracid is produced. It has low solubility and does not efficiently form peracid, which is disadvantageous in terms of production efficiency.
In addition, since only a low concentration peracid solution can be obtained, it is disadvantageous in terms of distribution and the like. Therefore, the acid anhydride such as succinic anhydride or adipic anhydride is exclusively used for the production of these peracids. Things are used as raw materials.

【0004】しかしながら、それら無水物から導かれた
過酸水溶液は高濃度の過酸を生成させることが出来る反
面、過酸が分解するに伴い、冷時に於いて難溶解性の母
体酸結晶を析出し易く、経時的な安定性或いは安全性の
観点からも問題を有するものであり、また原料無水物が
比較的高価であると言う経済的な理由も伴うため、特殊
な用途以外の一般的用途には殆ど利用されることがない
状態にある。
However, while the peracid aqueous solution derived from these anhydrides can generate a high concentration of peracid, as the peracid is decomposed, a hardly soluble mother acid crystal precipitates in the cold state. It is easy to do and has a problem from the viewpoint of stability over time or safety, and it is accompanied by the economical reason that the raw material anhydride is relatively expensive, so general applications other than special applications It is in a state where it is rarely used.

【0005】過グルタル酸については水溶解性の点で優
れているものの、殺菌その他利用面での効果が不十分で
あり、また原料となる純粋なグルタル酸がコハク酸やア
ジピン酸に比較して希少かつ高価であるため、原料の入
手或いは経済性の面でも一般的な利用がさらに困難なも
のとなっている。
Although perglutaric acid is excellent in water solubility, its effect on sterilization and other uses is insufficient, and pure glutaric acid as a raw material is compared with succinic acid and adipic acid. Since it is rare and expensive, it is more difficult to generally use the raw material and the economical aspect.

【0006】[0006]

【発明が解決しようとする課題】本発明の目的は、かか
る無臭、水低溶解性ジカルボン酸類から誘導される過ジ
カルボン酸含有水溶液の経時的変化に起因する欠点ある
いは製造効率や流通上の不利益性を改善し、また水易溶
性のグルタル酸から誘導される過グルタル酸水溶液の作
用効果或いは経済的課題を改善した、安定性或いは性能
や経済性に優れた汎用性の殺菌、漂白、洗浄用水溶液組
成物を提供する事にある。
DISCLOSURE OF THE INVENTION The object of the present invention is to provide a defect or a disadvantage in production efficiency and distribution due to the change with time of the perdicarboxylic acid-containing aqueous solution derived from such odorless, low-water-soluble dicarboxylic acids. For general purpose sterilization, bleaching and washing with stability or performance and economical efficiency, which has improved stability and improved action effect or economic problem of perglutaric acid aqueous solution derived from water-soluble glutaric acid. It is to provide an aqueous solution composition.

【0007】[0007]

【課題を解決するための手段】本発明者らは、これらの
問題点について鋭意研究を行った結果、水低溶解性のコ
ハク酸、アジピン酸に水易溶性のグルタル酸を混合し、
これら無臭性ジカルボン酸を溶解した複合ジカルボン酸
水溶液は、水低溶解性のコハク酸、アジピン酸を存在す
る水分に対してより高い濃度で溶解することが可能であ
り、該複合ジカルボン酸水溶液に過酸化水素を加えて反
応させることによって、グルタル酸の使用比率を低下さ
せても効率的な過ジカルボン酸の形成が行われ、経済面
での課題を改善出来ること、また得られる特定濃度組成
の過ジカルボン酸含有水溶液は利用に際しての作用効果
に優れ、貯蔵時に於いて結晶析出を起こし難いことを見
い出し、これによって単一ジカルボン酸から誘導された
無臭性過ジカルボン酸含有水溶液のもつ諸問題点が改善
され、安定性や安全性、或いはまた性能面や経済性に於
いてもより優れた過ジカルボン酸含有水溶液を得ること
ができることを見い出し本発明を完成させるに至った。
Means for Solving the Problems As a result of intensive studies on these problems, the inventors of the present invention mixed succinic acid and adipic acid having low water solubility with glutaric acid having high water solubility,
The complex dicarboxylic acid aqueous solution in which these odorless dicarboxylic acids are dissolved can dissolve succinic acid and adipic acid, which have low water solubility, at a higher concentration with respect to the existing water, and the complex dicarboxylic acid aqueous solution can be dissolved. By adding hydrogen oxide and reacting, even if the usage ratio of glutaric acid is reduced, efficient formation of perdicarboxylic acid is carried out, and it is possible to improve the economic problem and to obtain the desired concentration composition. It was found that the dicarboxylic acid-containing aqueous solution is excellent in action and effect during use and is less likely to cause crystal precipitation during storage, thereby improving various problems of the odorless perdicarboxylic acid-containing aqueous solution derived from a single dicarboxylic acid. Therefore, it is possible to obtain a perdicarboxylic acid-containing aqueous solution that is superior in terms of stability, safety, performance, and economy. This has led to the completion of the out of the present invention.

【0008】即ち、本願発明は、グルタル酸とコハク酸
とを含む複合ジカルボン酸と過酸化水素とを反応させて
得られる、(1)過ジカルボン酸(モノ過ジカルボン酸
換算)が 0.05 〜 1.0 モル/Kg溶液、(2)過ジカル
ボン酸を除く総ジカルボン酸類が 0.2 〜 2.2 モル/Kg
溶液、(3)過酸化水素が 1.0 〜12.0 モル/Kg溶液、
(4)安定剤が 0.01〜3.0重量%の濃度で含有され、
かつコハク酸(過コハク酸を含む)濃度が 0.1 〜 0.7
モル/Kg溶液の範囲で、またグルタル酸(過グルタル酸
を含む)1モルに対するコハク酸(過コハク酸を含む)
のモル比率が0.1〜2.0の割合で含有される過カルボン酸
含有水溶液、及び、グルタル酸とコハク酸及びアジピン
酸を含む複合ジカルボン酸と過酸化水素とを反応させて
得られる、(1)過ジカルボン酸(モノ過ジカルボン酸
換算)が 0.05 〜 1.0 モル/Kg溶液、(2)過ジカル
ボン酸を除く総ジカルボン酸類が 0.2 〜 2.2モル/Kg
溶液、(3)過酸化水素が 1.0 〜12.0 モル/Kg溶液、
(4)安定剤が 0.01〜3.0重量%の濃度で含有され、か
つコハク酸(過コハク酸を含む)濃度が 0.1 〜 0.7モ
ル/Kg溶液、アジピン酸(過アジピン酸を含む)濃度が
0.02〜0.2モル/Kg溶液の範囲で、またグルタル酸(過
グルタル酸を含む)1モルに対するその他ジカルボン酸
(それぞれの過ジカルボン酸を含む)合計のモル比率が
0.1〜2.0の割合で含有される過ジカルボン酸含有水溶
液、ならびにそれらの製造方法に関する。
That is, according to the present invention, (1) perdicarboxylic acid (converted to monoperdicarboxylic acid) obtained by reacting a complex dicarboxylic acid containing glutaric acid and succinic acid with hydrogen peroxide is 0.05 to 1.0 mol. / Kg solution, (2) Total dicarboxylic acids excluding perdicarboxylic acid 0.2 to 2.2 mol / Kg
Solution, (3) hydrogen peroxide 1.0-12.0 mol / Kg solution,
(4) Stabilizer is contained in a concentration of 0.01 to 3.0% by weight,
And the concentration of succinic acid (including persuccinic acid) is 0.1 to 0.7.
Succinic acid (including persuccinic acid) per mol of glutaric acid (including perglutaric acid) in the range of mol / Kg solution
(1) a percarboxylic acid-containing aqueous solution having a molar ratio of 0.1 to 2.0, and a complex dicarboxylic acid containing glutaric acid, succinic acid, and adipic acid, and hydrogen peroxide. Dicarboxylic acid (converted to monoperdicarboxylic acid) is 0.05 to 1.0 mol / Kg solution, (2) Total dicarboxylic acids excluding perdicarboxylic acid is 0.2 to 2.2 mol / Kg
Solution, (3) hydrogen peroxide 1.0-12.0 mol / Kg solution,
(4) The stabilizer is contained in a concentration of 0.01 to 3.0% by weight, the succinic acid (including persuccinic acid) concentration is 0.1 to 0.7 mol / Kg solution, and the adipic acid (including peradipic acid) concentration is
In the range of 0.02 to 0.2 mol / Kg solution, the total molar ratio of other dicarboxylic acids (including each perdicarboxylic acid) to 1 mol of glutaric acid (including perglutaric acid) is
The present invention relates to a perdicarboxylic acid-containing aqueous solution contained in a ratio of 0.1 to 2.0, and a method for producing them.

【0009】本発明の過ジカルボン酸含有水溶液は、グ
ルタル酸を必須とし、コハク酸さらにはアジピン酸を複
合させて使用し、これらのジカルボン酸類を水に溶解さ
せて所定の濃度、比率のジカルボン酸水溶液とし、当該
水溶液をさらにイオン交換樹脂等により処理精製して、
含有される重金属を除去した後、安定剤の共存下に過酸
化水素溶液を添加、反応させて調製するが、必要に応じ
てさらに脱イオン水等で希釈して所望の濃度とすること
が出来る。
The perdicarboxylic acid-containing aqueous solution of the present invention requires glutaric acid as an essential component, and is used by combining succinic acid and adipic acid. These dicarboxylic acids are dissolved in water to prepare dicarboxylic acid having a predetermined concentration and ratio. An aqueous solution, which is further treated and purified with an ion exchange resin,
After removing the contained heavy metals, a hydrogen peroxide solution is added and reacted in the presence of a stabilizer to prepare it, but it can be further diluted with deionized water or the like to a desired concentration if necessary. .

【0010】本発明で使用する複合ジカルボン酸水溶液
は、基本的にはグルタル酸、コハク酸、アジピン酸等を
それぞれ単一純粋な形で使用し、これらを所望の濃度、
比率で水に溶解させて複合ジカルボン酸水溶液を調製す
るが、既にこれらジカルボン酸類が定比、不定比で混合
した形の粗ジカルボン酸類は入手が容易であり、工業的
にはこれらを原料として複合ジカルボン酸水溶液を調製
することが有利である。この場合には、一旦、水に加温
溶解させた後に冷却して、低溶解性ジカルボン酸の不要
部分を晶析させ、分離除去する方法や、混合ジカルボン
酸類を水に懸濁させ不溶解部分を分離除去する方法、或
いは混合されたジカルボン酸と単一ジカルボン酸を混合
使用する等の方法で各ジカルボン酸の濃度或いは比率を
調整し、所望とする複合ジカルボン酸水溶液を調製す
る。この他、特に望む場合に於いてはこれらジカルボン
酸類の無水物を使用し、水に溶解、水和させて用いるこ
とも出来る。
The complex dicarboxylic acid aqueous solution used in the present invention basically comprises glutaric acid, succinic acid, adipic acid and the like in a single pure form, and these are used in a desired concentration,
A complex dicarboxylic acid aqueous solution is prepared by dissolving it in water at a ratio, but crude dicarboxylic acids in the form of a mixture of these dicarboxylic acids in stoichiometric and non-stoichiometric ratios are readily available, and industrially, these are used as raw materials for complexing. It is advantageous to prepare an aqueous dicarboxylic acid solution. In this case, once dissolved in water by heating and then cooled, the unnecessary portion of the low-solubility dicarboxylic acid is crystallized, separated and removed, or the mixed dicarboxylic acids are suspended in water and the insoluble portion is removed. The concentration or ratio of each dicarboxylic acid is adjusted by a method of separating and removing the above or a method of mixing and using the mixed dicarboxylic acid and a single dicarboxylic acid to prepare a desired aqueous solution of the complex dicarboxylic acid. In addition, if desired, the anhydrides of these dicarboxylic acids can be used by dissolving and hydrating in water.

【0011】コハク酸或いはアジピン酸など低溶解性ジ
カルボン酸類の水への溶解量はグルタル酸の共存によっ
て表1の様に増加し、これによって複合ジカルボン酸水
溶液中に存在する低溶解性ジカルボン酸類の溶解比率を
増加させることができ、また、より少ない水に多くのジ
カルボン酸類を溶解させることが出来るため、平衡反応
である過ジカルボン酸の反応をより有利に行うことが可
能となる。
The amount of low-solubility dicarboxylic acids such as succinic acid or adipic acid dissolved in water increases as shown in Table 1 due to the coexistence of glutaric acid, whereby the low-solubility dicarboxylic acids existing in the aqueous solution of complex dicarboxylic acids are increased. Since the dissolution ratio can be increased and a large amount of dicarboxylic acids can be dissolved in less water, the equilibrium reaction of perdicarboxylic acid can be carried out more advantageously.

【0012】[0012]

【表1】 [Table 1]

【0013】複合ジカルボン酸水溶液中のジカルボン酸
濃度は、目的とする最終過ジカルボン酸含有水溶液の組
成に関連し、反応の際に加えられる過酸化水素のジカル
ボン酸に対する比率或いは使用する過酸化水素の濃度等
が選択されるため一概に特定することは出来ないが、一
般的には当該ジカルボン酸水溶液のイオン交換樹脂或い
はキレート樹脂による精製操作の操作性や重金属類の除
去効率或いはまた目的とする過ジカルボン酸の生成効率
から、ジカルボン酸濃度として2〜6モル/Kg溶液、好
ましくは3〜5モル/Kg溶液としてイオン交換樹脂によ
る処理に供する。
The concentration of the dicarboxylic acid in the complex aqueous solution of dicarboxylic acid is related to the composition of the final aqueous solution containing the perdicarboxylic acid, and the ratio of hydrogen peroxide to dicarboxylic acid added during the reaction or the amount of hydrogen peroxide used. Since the concentration and other factors are selected, it cannot be specified unconditionally, but generally, the operability of the purification operation of the dicarboxylic acid aqueous solution using an ion exchange resin or a chelate resin, the efficiency of removing heavy metals, and / or the target According to the production efficiency of the dicarboxylic acid, the concentration of the dicarboxylic acid is 2 to 6 mol / Kg solution, preferably 3 to 5 mol / Kg solution, which is subjected to the treatment with the ion exchange resin.

【0014】原料となるジカルボン酸は、通常、不純物
として微量の重金属を含有し、ジカルボン酸と過酸化水
素との反応の際に共存することによって、過ジカルボン
酸の形成を阻害し、目的とする濃度の過ジカルボン酸が
得られない場合や、そのまま最終過ジカルボン酸含有水
溶液中に存在することによって過ジカルボン酸或いは過
酸化水素の分解を促進し、保存安定性を低下させる等、
実用上の問題を生起させるため、これら金属イオンを除
去する目的から、ジカルボン酸類を水溶液とした後にイ
オン交換樹脂或いはキレート樹脂によって処理し、当該
複合ジカルボン酸水溶液中の鉄、銅、ニッケル、クロ
ム、マンガン、亜鉛の総重金属イオン濃度を2mg/Kg溶
液以下に低下させる。ここでのイオン交換樹脂としては
スルホン酸基をイオン交換性官能基とする一般公知の強
酸性陽イオン交換樹脂を好適に使用することができ、ま
た、キレート樹脂としてはイミノジ酢酸基を有する、或
いはまたポリアミン型の一般公知キレート樹脂が利用出
来る。ジカルボン酸水溶液中の金属類の除去は陽イオン
交換樹脂或いはキレート樹脂による処理を行うことでお
およそ目的とする金属除去を行うことが出来るが、最終
的に得られる過ジカルボン酸含有水溶液をより高度に安
定化することを望む場合には、さらに陰イオン交換樹脂
を陽イオン交換樹脂処理前に併用し、陰イオン状態の微
量金属を除去することによってさらに良好な保存安定性
を得ることが出来る。
The dicarboxylic acid as a raw material usually contains a trace amount of a heavy metal as an impurity and coexists during the reaction of the dicarboxylic acid with hydrogen peroxide to inhibit the formation of the perdicarboxylic acid, and is aimed at. If a concentration of perdicarboxylic acid cannot be obtained, or if it exists in the final perdicarboxylic acid-containing aqueous solution as it is, the decomposition of perdicarboxylic acid or hydrogen peroxide is promoted, and the storage stability is lowered.
In order to cause practical problems, for the purpose of removing these metal ions, dicarboxylic acids are treated with an ion exchange resin or a chelate resin after being made into an aqueous solution, and iron, copper, nickel, chromium in the aqueous solution of the composite dicarboxylic acid, The total heavy metal ion concentration of manganese and zinc is lowered to 2 mg / Kg solution or less. As the ion exchange resin here, a generally known strongly acidic cation exchange resin having a sulfonic acid group as an ion exchange functional group can be preferably used, and as the chelate resin, an iminodiacetic acid group is contained, or In addition, polyamine type generally known chelating resins can be used. The removal of metals from the aqueous solution of dicarboxylic acid can be performed by treating with a cation exchange resin or a chelate resin, and the target metal can be removed. If stabilization is desired, a further better storage stability can be obtained by further using an anion exchange resin before the cation exchange resin treatment to remove a trace amount of metal in the anion state.

【0015】イオン交換樹脂或いはキレート樹脂による
原料ジカルボン酸水溶液の処理は、ジカルボン酸水溶液
中に当該樹脂を懸濁させ濾過分離する方法、或いは当該
樹脂を充填した充填塔を通液する方法等の一般常法に従
って実施され、処理時に於けるジカルボン酸類の結晶析
出を避けるためには、処理液中のジカルボン酸濃度を処
理温度に於ける飽和濃度以下として実施し、前記重金属
類濃度を2.0mg/kg以下、望ましくは1.0mg/kg以下のジカ
ルボン酸水溶液として過酸化水素との反応に供する。処
理後の陽イオン交換樹脂は希硫酸等の鉱酸水溶液で再生
して循環使用される。
Treatment of the raw material dicarboxylic acid aqueous solution with an ion exchange resin or a chelate resin is generally carried out by suspending the resin in the dicarboxylic acid aqueous solution and separating it by filtration, or by passing it through a packed column filled with the resin. It is carried out according to a conventional method, and in order to avoid crystal precipitation of dicarboxylic acids during the treatment, the concentration of the dicarboxylic acid in the treatment liquid is set to be equal to or lower than the saturation concentration at the treatment temperature, and the concentration of the heavy metals is 2.0 mg / kg. Hereinafter, it is desirably used as a 1.0 mg / kg or less aqueous solution of dicarboxylic acid for reaction with hydrogen peroxide. The cation exchange resin after the treatment is reused by recycling it with an aqueous solution of a mineral acid such as dilute sulfuric acid.

【0016】本発明に於ける過ジカルボン酸の生成は、
安定剤の共存下に上記の方法で精製された複合ジカルボ
ン酸水溶液と過酸化水素水溶液とを混合し、攪拌下に反
応させる方法で行われ、所望する場合には反応時に脱イ
オン水を添加して希釈或いは固形ジカルボン酸をさらに
添加する等の方法で濃度を調整することができる。反応
は 0〜30℃と言った低温度で長時間反応させることで実
施することも出来るが、工業的な製造としては効率的で
はないため、通常は反応速度を増加させる目的から 30
〜80℃、好ましくは40〜60℃に加温して実施され、ま
た、所望する場合には必要に応じて硫酸、リン酸、縮合
リン酸類、ホスホン酸類の様な酸性物質を触媒として反
応液Kg当たり1〜10gの割合で添加することによってさら
に反応時間を短縮することが出来る。
The production of perdicarboxylic acid in the present invention is as follows.
It is carried out by a method in which a complex dicarboxylic acid aqueous solution purified by the above method and a hydrogen peroxide aqueous solution are mixed in the presence of a stabilizer and reacted with stirring, and deionized water is added at the time of reaction if desired. The concentration can be adjusted by a method such as dilution or addition of a solid dicarboxylic acid. The reaction can be carried out by reacting at a low temperature such as 0 to 30 ° C. for a long time, but it is not efficient as an industrial production, and therefore it is usually performed for the purpose of increasing the reaction rate.
To 80 ° C, preferably 40 to 60 ° C, and if necessary, a reaction solution using an acidic substance such as sulfuric acid, phosphoric acid, condensed phosphoric acids, or phosphonic acids as a catalyst, if necessary. The reaction time can be further shortened by adding 1 to 10 g per Kg.

【0017】反応に際し高温の反応温度が許容されるた
めには反応液が高度に安定化されていることが必要であ
り、原料ジカルボン酸水溶液の精製が不十分である場
合、あるいは安定剤量が不十分であるような場合には、
生成される過ジカルボン酸が高温下に於いて速やかに分
解される結果、希望した濃度の過ジカルボン酸溶液を得
ることが出来ない。反応の時間は、通常、2〜80時間、
好ましくは 4〜50時間で行われるが、反応後に於いて反
応液を希釈して最終組成液とする場合などの様に、必要
とする最終的な過ジカルボン酸濃度が低い場合等は、反
応時間として必ずしも平衡組成に達するまでの時間に制
約されることなく短縮して実施することが出来る。
In order to allow a high reaction temperature in the reaction, it is necessary that the reaction solution is highly stabilized. If the raw material aqueous solution of dicarboxylic acid is not sufficiently purified, or the amount of the stabilizer is insufficient. If it seems to be insufficient,
As a result, the produced perdicarboxylic acid is rapidly decomposed at a high temperature, so that a perdicarboxylic acid solution having a desired concentration cannot be obtained. The reaction time is usually 2 to 80 hours,
It is preferably carried out for 4 to 50 hours, but when the final concentration of the required perdicarboxylic acid is low, such as when the reaction solution is diluted to give the final composition after the reaction, the reaction time As a result, the time required for reaching the equilibrium composition can be shortened without being restricted.

【0018】反応に際して混合するジカルボン酸と過酸
化水素との比率は、目的とする最終組成液の組成に関連
して使用する比率を任意に選択し得るが、反応液中のジ
カルボン酸濃度を一定とした場合、ジカルボン酸に対す
る過酸化水素の比率を増加させる程、生成する過ジカル
ボン酸の割合或いは濃度は増加し、過ジカルボン酸の生
成という点では効率的であるものの、同時に過酸化水素
の濃度も上昇するため、過酸化物濃度の上昇によって最
終組成液の取り扱い或いは貯蔵時に於ける潜在的危険性
も増加するため、必要以上の多量を用いることは好まし
くない。また必要以上に低比率として用いることも過ジ
カルボン酸の生成率が低下する点で効率的でないため、
本発明でのジカルボン酸に対する過酸化水素のモル比率
は0.2〜15、好ましくは0.5〜10とする。使用される過酸
化水素の濃度は、取り扱い或いは危険性の観点から、通
常、10〜70重量%として使用するが、高濃度の過ジカル
ボン酸の生成を望む場合に於いては生成効率の点でより
高濃度で使用するのが有利である。
The ratio of the dicarboxylic acid and hydrogen peroxide to be mixed in the reaction can be arbitrarily selected in relation to the composition of the target final composition liquid, but the concentration of the dicarboxylic acid in the reaction liquid is constant. In the case of, when the ratio of hydrogen peroxide to dicarboxylic acid is increased, the ratio or concentration of perdicarboxylic acid produced increases, and although it is efficient in terms of production of perdicarboxylic acid, the concentration of hydrogen peroxide is also increased. Therefore, it is not preferable to use a larger amount than necessary because the increase in the peroxide concentration also increases the potential risk during handling or storage of the final composition liquid. In addition, it is not efficient to use a lower ratio than necessary because the production rate of perdicarboxylic acid decreases.
The molar ratio of hydrogen peroxide to dicarboxylic acid in the present invention is 0.2 to 15, preferably 0.5 to 10. The concentration of hydrogen peroxide used is usually 10 to 70% by weight from the viewpoint of handling or danger.However, in the case where a high concentration of perdicarboxylic acid is desired to be produced, in terms of production efficiency. It is advantageous to use higher concentrations.

【0019】反応に際して添加される安定剤としては、
アミノトリ(メチレンホスホン酸)、1-ヒドロキシエチ
リデン-1,1-ジホスホン酸、エチレンジアミンテトラ
(メチレンホスホン酸)等の様な有機ホスホン酸或いは
ピコリン酸、ジピコリン酸、キノリン酸等の様なピリジ
ンカルボン酸類が適当であり、反応混合物に対して0.01
〜3.0重量%、好ましくは0.05〜1.0重量%の割合で添加
して反応を行う。
The stabilizer added during the reaction is
Organic phosphonic acids such as aminotri (methylenephosphonic acid), 1-hydroxyethylidene-1,1-diphosphonic acid, ethylenediaminetetra (methylenephosphonic acid) or pyridinecarboxylic acids such as picolinic acid, dipicolinic acid, quinolinic acid Suitable, 0.01 for the reaction mixture
~ 3.0 wt%, preferably 0.05-1.0 wt% is added to carry out the reaction.

【0020】反応によって得られる過ジカルボン酸含有
水溶液はそのまま最終的な組成液とするか、望む場合に
は重金属類を除去した水やジカルボン酸類等を添加し、
所定濃度範囲の水溶液とする。該過ジカルボン酸含有水
溶液はそこに含有されるジカルボン酸類、過酸化水素、
水の各成分濃度によって最終的にはその平衡組成に変化
し、ジカルボン酸類の濃度が高い程より高い過ジカルボ
ン酸濃度が許容されるものの、必要以上に高くした場合
には冷時に結晶を析出する等の問題を生じ易く、また、
低すぎる場合には過ジカルボン酸濃度も必要以上に低下
することになるため、過ジカルボン酸を除くジカルボン
酸類としては 0.2 〜 2.2モル/Kg溶液、好ましくは 0.
3〜1.8モル/Kg溶液とする。また、過酸化水素濃度につ
いてもその濃度が高い程より高い過ジカルボン酸濃度が
許容されるものの、過酸化水素、過ジカルボン酸濃度を
高める程、該水溶液の潜在的危険性が増加することによ
って、その利用が制約される問題を生じるため、これら
については過酸化水素として 1.0 〜12モル/Kg溶液、
好ましくは 1.5〜10モル/Kg溶液の濃度に、また過ジカ
ルボン酸(モノ過ジカルボン酸換算)濃度については
0.05 〜 1.0モル/Kg溶液、好ましくは 0.10〜0.8モル
/Kg溶液の範囲で含有させるのが良い。
The perdicarboxylic acid-containing aqueous solution obtained by the reaction is used as it is as a final composition liquid, or if desired, water and dicarboxylic acids from which heavy metals have been removed are added,
Use an aqueous solution with a predetermined concentration range. The perdicarboxylic acid-containing aqueous solution contains dicarboxylic acids, hydrogen peroxide,
Ultimately, the equilibrium composition changes depending on the concentration of each component of water, and higher perdicarboxylic acid concentrations are permissible as the concentration of dicarboxylic acids increases, but if it is made higher than necessary, crystals will precipitate in the cold. It is easy to cause problems such as
If it is too low, the concentration of perdicarboxylic acid will be reduced more than necessary. Therefore, as dicarboxylic acids excluding perdicarboxylic acid, 0.2 to 2.2 mol / Kg solution, preferably 0.
3 to 1.8 mol / Kg solution. Regarding the concentration of hydrogen peroxide, a higher concentration of perdicarboxylic acid is allowed as the concentration is higher, but as the concentration of hydrogen peroxide or perdicarboxylic acid is increased, the potential risk of the aqueous solution is increased. Because of the problem that its utilization is restricted, 1.0 to 12 mol / Kg solution of hydrogen peroxide,
Preferably, the concentration of the solution is 1.5 to 10 mol / Kg, and the concentration of perdicarboxylic acid (in terms of monoperdicarboxylic acid) is
It is preferable to add it in the range of 0.05 to 1.0 mol / Kg solution, preferably 0.10 to 0.8 mol / Kg solution.

【0021】本発明による過カルボン酸含有水溶液中の
グルタル酸、コハク酸或いはアジピン酸濃度は該水溶液
からの結晶析出等の経時安定性に関連した重要な要因で
あり、冷時に於けるこれら結晶の析出を避けるために、
コハク酸(過コハク酸を含む)濃度については 0.1 〜
0.7モル/Kg溶液、アジピン酸(過アジピン酸を含む)
濃度については 0.02〜0.2モル/Kg溶液の範囲とし、
またグルタル酸(過グルタル酸を含む)1モルに対する
その他ジカルボン酸(それぞれの過ジカルボン酸を含
む)合計のモル比率は0.1〜2.0の割合で含有される様に
する。
The concentration of glutaric acid, succinic acid or adipic acid in the percarboxylic acid-containing aqueous solution according to the present invention is an important factor related to stability over time such as crystal precipitation from the aqueous solution, and the concentration of these crystals in the cold state. To avoid precipitation
Concentration of succinic acid (including persuccinic acid) 0.1 ~
0.7 mol / Kg solution, adipic acid (including peradipic acid)
Regarding the concentration, range from 0.02 to 0.2 mol / Kg solution,
Further, the total molar ratio of other dicarboxylic acids (including respective perdicarboxylic acids) to 1 mol of glutaric acid (including perglutaric acid) is set to be 0.1 to 2.0.

【0022】本発明の過カルボン酸水溶液には、望む場
合に於いて本発明の目的を妨げない範囲で界面活性剤、
香料、着色剤等の添加物を添加、含有させることが出来
る。
In the aqueous solution of percarboxylic acid of the present invention, a surfactant, if desired, within a range not impairing the object of the present invention,
Additives such as fragrances and colorants can be added and contained.

【0023】[0023]

【発明の効果】本発明による過ジカルボン酸水溶液は、
コハク酸、アジピン酸等低溶解性ジカルボン酸を単独使
用する方法に比較し、得られる過ジカルボン酸濃度をよ
り高濃度となし得る点で効率的であるばかりでなく、冷
時に於いてこれら低溶解性ジカルボン酸の結晶を析出し
難い等、経時安定性が改善されている点でより実用性に
優れ、さらにその作用効果に於いてもグルタル酸単一か
ら得られる過カルボン酸溶液よりもより効果的である
等、それぞれ単一のジカルボン酸から誘導された過ジカ
ルボン酸含有水溶液それぞれの欠点が改善され、物性、
作用性、或いは経済性に於いてより実用性に優れた殺
菌、漂白、洗浄用過カルボン酸含有水溶液組成物を得る
ことが出来る。
The perdicarboxylic acid aqueous solution according to the present invention is
Compared with the method of using low-solubility dicarboxylic acid such as succinic acid and adipic acid alone, it is not only efficient in that the concentration of perdicarboxylic acid obtained can be made higher, but these low-solubility in cold state It is more practical than the percarboxylic acid solution obtained from glutaric acid alone, and is more effective than the percarboxylic acid solution obtained from a single glutaric acid. The physical properties of the perdicarboxylic acid-containing aqueous solution derived from a single dicarboxylic acid are improved,
It is possible to obtain a percarboxylic acid-containing aqueous solution composition for sterilization, bleaching and washing which is more practical in terms of action and economy.

【0024】[0024]

【実施例】以下に、実施例及び比較例をもって本発明を
説明する。
EXAMPLES The present invention will be described below with reference to Examples and Comparative Examples.

【0025】実施例1〜3 水にコハク酸、アジピン酸、グルタル酸を加え、50℃に
加温して攪拌、溶解させ、これらジカルボン酸類の混合
したコハク酸 0.5〜0.8モル/Kg、アジピン酸0.1〜0.3
モル/Kg、グルタル酸 0.6〜2.9モル/Kgの濃度で含有
する水溶液を調製し、次いでこれら溶液をポリスチレン
スルホン酸型強酸性陽イオン交換樹脂(オルカ゛ノ製,アンハ゛ーラ
イトIR-124)を充填したカラムに、30℃、SV比 4〜6で
通液し、重金属類の含有率を 1.0mg/Kg溶液以下とした
複合ジカルボン酸水溶液を調製した。さらにこれら溶液
に60重量%過酸化水素水溶液と安定剤の1-ヒドロキシエ
チリデン-1,1-ジホスホン酸60重量%水溶液を添加して
各成分の初濃度を表2に示した値となし、50℃で72時間
反応させた。得られた反応液中の過カルボン酸及び過酸
化水素濃度、及びこれら組成液を 2〜3℃で4日間放置
した場合の結晶析出の有無を観察した結果は表2に示し
た。
Examples 1 to 3 Succinic acid, adipic acid and glutaric acid were added to water, heated at 50 ° C., stirred and dissolved, and succinic acid mixed with these dicarboxylic acids 0.5 to 0.8 mol / Kg, adipic acid 0.1 to 0.3
A column filled with an aqueous solution containing mol / Kg and glutaric acid at a concentration of 0.6 to 2.9 mol / Kg, and then filled with a polystyrene sulfonic acid type strongly acidic cation exchange resin (Amberlite IR-124, manufactured by Olgano). At 30 ° C. and an SV ratio of 4 to 6, the aqueous solution of complex dicarboxylic acid having a heavy metal content of 1.0 mg / Kg or less was prepared. Furthermore, 60% by weight aqueous solution of hydrogen peroxide and 60% by weight aqueous solution of stabilizer 1-hydroxyethylidene-1,1-diphosphonic acid were added to these solutions to obtain the initial concentrations of the respective components as shown in Table 2. The reaction was carried out at ℃ for 72 hours. Table 2 shows the results of observing the concentration of percarboxylic acid and hydrogen peroxide in the obtained reaction solution, and the presence or absence of crystal precipitation when these composition solutions were allowed to stand at 2 to 3 ° C. for 4 days.

【0026】実施例4 コハク酸、グルタル酸を用いた以外は実施例1〜3と同
様に、コハク酸 0.7モル/Kg、グルタル酸 0.9モル/Kg
の濃度で含有する水溶液を調製し、同様にイオン交換樹
脂処理を行った後、過酸化水素溶液、安定剤を添加して
初期濃度がコハク酸、グルタル酸、過酸化水素について
0.50モル/Kg、0.73モル/Kg、4.37モル/Kgの溶液を
調製し、これらを反応させた結果についても表2に示し
た。
Example 4 As in Examples 1 to 3, except that succinic acid and glutaric acid were used, succinic acid 0.7 mol / Kg and glutaric acid 0.9 mol / Kg
After preparing an aqueous solution containing it at the same concentration and treating it with an ion-exchange resin in the same way, add a hydrogen peroxide solution and a stabilizer to obtain initial concentrations of succinic acid, glutaric acid, and hydrogen peroxide.
Table 2 also shows the results of preparing 0.50 mol / Kg, 0.73 mol / Kg and 4.37 mol / Kg solutions and reacting them.

【0027】[0027]

【表2】 [Table 2]

【0028】比較例1〜2 水にコハク酸を加え、50℃に加温して攪拌、溶解させ、
コハク酸濃度0.60モル/Kg、及び0.75モル/Kgの溶液を
調製し、この溶液を実施例1〜3と同様にして陽イオン
交換樹脂で処理した。さらにこれら溶液に60重量%過酸
化水素水溶液と安定剤の1-ヒドロキシエチリデン-1,1-
ジホスホン酸60重量%水溶液を添加して各成分の初濃度
をコハク酸、過酸化水素についてそれぞれ 0.45モル/K
g、4.2モル/Kg、及び 0.56モル/Kg、4.5モル/Kgの溶
液を調製し、これを実施例1〜3と同様にして反応させ
平衡溶液とした後、生成した過コハク酸を分析し、次い
でこの溶液を2〜3℃で放置貯蔵し、結晶析出の状態を観
察した。その結果は表2に示した様なものであり、生成
した過カルボン酸濃度は低く、また実施例1〜3と総コ
ハク酸濃度が同等或いは低いにも拘わらず数日間で結晶
の析出が観察された。
Comparative Examples 1-2 Succinic acid was added to water, heated to 50 ° C., stirred and dissolved,
Solutions having succinic acid concentrations of 0.60 mol / Kg and 0.75 mol / Kg were prepared, and this solution was treated with a cation exchange resin in the same manner as in Examples 1 to 3. Furthermore, 60 wt% hydrogen peroxide solution and stabilizer 1-hydroxyethylidene-1,1-
The initial concentration of each component was 0.45 mol / K for succinic acid and hydrogen peroxide by adding 60% by weight diphosphonic acid aqueous solution.
g, 4.2 mol / Kg, and 0.56 mol / Kg, 4.5 mol / Kg solutions were prepared and reacted in the same manner as in Examples 1 to 3 to prepare equilibrium solutions, and the generated persuccinic acid was analyzed. Then, this solution was allowed to stand at 2-3 ° C. for storage, and the state of crystal precipitation was observed. The results are shown in Table 2, and the concentration of the generated percarboxylic acid was low, and the precipitation of crystals was observed in several days even though the total succinic acid concentration was the same as or lower than those in Examples 1 to 3. Was done.

【0029】比較例3 コハク酸をアジピン酸に換え、アジピン酸濃度0.18モル
/Kgの溶液を調製し、比較例1と同様に処理して初期濃
度がアジピン酸、過酸化水素についてそれぞれ0.13モル
/Kg、4.31モル/Kgの溶液を調製し、これを実施例1〜
3と同様にして反応させ平衡溶液とした後、生成した過
アジピン酸を分析し、次いでこの溶液を2〜3℃で放置貯
蔵し、結晶析出の状態を観察した。その結果は表2に示
した様なものであり、生成した過カルボン酸濃度も低
く、また実施例1〜2と総アジピン酸濃度が低いにも拘
わらず数日間で結晶の析出が観察された。
COMPARATIVE EXAMPLE 3 Adipic acid was used instead of succinic acid to prepare a solution having an adipic acid concentration of 0.18 mol / Kg, and the same treatment as in Comparative Example 1 was performed to obtain initial concentrations of adipic acid and hydrogen peroxide of 0.13 mol / Kg, respectively. A solution of Kg, 4.31 mol / Kg was prepared, which was used in Examples 1 to 1.
After reacting in the same manner as in 3 to make an equilibrium solution, the produced peradipic acid was analyzed, and then this solution was left to stand at 2 to 3 ° C. for storage to observe the state of crystal precipitation. The results are shown in Table 2, and the concentration of the generated percarboxylic acid was low, and although the concentration of total adipic acid was low as in Examples 1 and 2, precipitation of crystals was observed in several days. .

【0030】比較例4 コハク酸をグルタル酸に換え、グルタル酸濃度0.67モル
/Kgの溶液を調製し、比較例1と同様に処理して初期濃
度がグルタル酸、過酸化水素について 0.50モル/Kg、
4.38モル/Kgの溶液を調製し、これらを実施例1〜3と
同様にして反応させ、生成した過グルタル酸濃度を分析
した結果、表2に示した如く0.11モル/Kgであった。
Comparative Example 4 A solution having a glutaric acid concentration of 0.67 mol / Kg was prepared by replacing succinic acid with glutaric acid, and treated in the same manner as in Comparative Example 1, and the initial concentration was 0.50 mol / Kg for glutaric acid and hydrogen peroxide. ,
A solution of 4.38 mol / Kg was prepared and reacted in the same manner as in Examples 1 to 3, and the concentration of the produced perglutaric acid was analyzed. As a result, as shown in Table 2, it was 0.11 mol / Kg.

【0031】実施例5 コハク酸、グルタル酸、アジピン酸がそれぞれ 25重量
%、64重量%、11重量%の割合で含有される粗ジカルボ
ン酸を原料とし、この1.1重量部に水1重量部を加
え、50℃に加温し、攪拌溶解させた後、溶液を0〜3℃に
冷却し、析出する結晶を濾過分離してコハク酸、グルタ
ル酸、アジピン酸がそれぞれ 0.76モル/Kg、 2.71モ
ル/Kg、0.15モル/Kgの濃度で含有する複合ジカルボン
酸溶液を調製した。次いでこの溶液をポリスチレンスル
ホン酸型強酸性陽イオン交換樹脂(オルカ゛ノ製,アンハ゛ーライトIR
-124)を充填したカラムに、室温下、SV比 5〜8で通
液し、重金属類の含有率を1.0mg/Kg溶液以下(Fe,Cu,N
i,Mn,Zn,Crの総濃度は 0.9mg/Kg溶液、Cu,Mn,Znについ
ては各0.04mg/Kg以下であった)の溶液とし、過酸化水
素との反応に供した。反応は樹脂処理を行った複合ジカ
ルボン酸溶液100重量部と44重量%の過酸化水素溶液68.
7重量部及び安定剤1-ヒドロキシエチリデン-1,1-ジホス
ホン酸60重量%水溶液0.33重量部とを混合し、コハク
酸、グルタル酸、アジピン酸及び過酸化水素の各初期濃
度が、それぞれ 0.45モル/Kg、1.61モル/Kg、0.09モ
ル/Kg及び 5.26モル/Kgとし、また、安定剤(純分)
を 0.12重量%の濃度として、50℃に加温下、攪拌を行
いつつ72時間実施した。反応後の溶液は、過ジカルボン
酸を 0.78モル/Kg、過ジカルボン酸を除いたジカルボ
ン酸が 1.34モル/Kg、過酸化水素 4.28モル/Kgの濃度
で含有した。尚、この溶液中のコハク酸(過コハク酸を
含む)、アジピン酸(過アジピン酸を含む)、グルタル
酸(過グルタル酸を含む)の各濃度は初濃度に同一であ
り、グルタル酸に対するその他のジカルボン酸のモル比
率は 0.35であった。この溶液を 0〜3℃下に4日間貯蔵
したが結晶の析出は観察されづ、また、50℃の温度で7
日間貯蔵した場合に於ける過酸化物成分の残存率は 95.
6%であった。
Example 5 A crude dicarboxylic acid containing succinic acid, glutaric acid, and adipic acid in proportions of 25% by weight, 64% by weight, and 11% by weight, respectively, was used as a raw material. Parts, heated to 50 ° C., dissolved with stirring, then cooled to 0 to 3 ° C., the precipitated crystals were separated by filtration to obtain succinic acid, glutaric acid, and adipic acid at 0.76 mol / Kg, respectively. A complex dicarboxylic acid solution containing 2.71 mol / Kg and 0.15 mol / Kg was prepared. Next, this solution was used as a polystyrene sulfonic acid type strong acid cation exchange resin (manufactured by Organo, Amberlite IR
-124) is passed through a column packed with -124) at room temperature with an SV ratio of 5 to 8 and the content of heavy metals is 1.0 mg / Kg solution or less (Fe, Cu, N
The total concentration of i, Mn, Zn, and Cr was 0.9 mg / Kg solution, and Cu, Mn, and Zn were 0.04 mg / Kg or less), and the solution was used for reaction with hydrogen peroxide. The reaction is 100 parts by weight of resin-treated complex dicarboxylic acid solution and 44% by weight hydrogen peroxide solution 68.
7 parts by weight and a stabilizer 1-hydroxyethylidene-1,1-diphosphonic acid 60% by weight aqueous solution 0.33 parts by weight are mixed, and each initial concentration of succinic acid, glutaric acid, adipic acid and hydrogen peroxide is 0.45 mol. / Kg, 1.61 mol / Kg, 0.09 mol / Kg and 5.26 mol / Kg, and stabilizer (pure content)
At a concentration of 0.12% by weight, and the mixture was heated at 50 ° C for 72 hours with stirring. The solution after the reaction contained 0.78 mol / Kg of perdicarboxylic acid, 1.34 mol / Kg of dicarboxylic acid excluding perdicarboxylic acid, and 4.28 mol / Kg of hydrogen peroxide. The concentrations of succinic acid (including persuccinic acid), adipic acid (including peradipic acid), and glutaric acid (including perglutaric acid) in this solution are the same as the initial concentration. The molar ratio of dicarboxylic acid was 0.35. The solution was stored at 0 to 3 ° C for 4 days, but no precipitation of crystals was observed.
The residual rate of peroxide components after storage for 95 days is 95.
It was 6%.

【0032】実施例6 コハク酸、グルタル酸、アジピン酸がそれぞれ 25重量
%、64重量%、11重量%の割合で含有される粗ジカルボ
ン酸を原料とし、この1.1重量部に水1重量部を加
え、50℃に加温し、攪拌溶解させ、コハク酸、グルタル
酸、アジピン酸がそれぞれ 1.02モル/Kg、 2.20モル
/Kg、0.34モル/Kgの濃度で含有する複合ジカルボン酸
溶液を調製した。次いでこの溶液を室温下、アクリル系
強塩基性陰イオン交換樹脂(オルカ゛ノ製,アンハ゛ーライトIRA-45
8)を充填したカラムに、SV比 10で、引き続いてポリ
スチレンスルホン酸型強酸性陽イオン交換樹脂(オルカ゛ノ
製,アンハ゛ーライトIR-124)を充填したカラムに、SV比 5で
通液し、複合ジカルボン酸溶液中の重金属を除去した後
(処理液中の Fe,Cu,Ni,Mn,Zn,Crの総濃度は 0.6mg/Kg
溶液、Cu,Mn,Znについては各0.04mg/Kg以下であっ
た)、この溶液 100重量部に対し12.6重量%の過酸化水
素水溶液 100重量部及び安定剤として1-ヒドロキシエチ
リデン-1,1-ジホスホン酸60重量%水溶液0.50重量部と
を混合し、コハク酸、グルタル酸、アジピン酸及び過酸
化水素の各初期濃度が、それぞれ 0.51モル/Kg、1.10
モル/Kg、0.16モル/Kg及び 1.85モル/Kgとし、ま
た、安定剤(純分)を 0.15重量%の濃度として、50℃
に加温下、攪拌を行いつつ72時間反応を行った。反応後
の溶液は、過ジカルボン酸を 0.18モル/Kg、過ジカル
ボン酸を除いたジカルボン酸が 1.59モル/Kg、過酸化
水素 1.66モル/Kgの濃度で含有した。尚、この溶液中
のコハク酸(過コハク酸を含む)、アジピン酸(過アジ
ピン酸を含む)、グルタル酸(過グルタル酸を含む)の
各濃度は初濃度に同一であり、グルタル酸に対するその
他のジカルボン酸のモル比率は 0.61であった。この溶
液を 0〜3℃下に4日間貯蔵したが結晶の析出は観察さ
れづ、また、50℃で7日間貯蔵した場合に於ける過酸化
物成分の残存率は 97.9%であった。
Example 6 A crude dicarboxylic acid containing succinic acid, glutaric acid, and adipic acid in the proportions of 25% by weight, 64% by weight, and 11% by weight, respectively, was used as a raw material. Parts, heated to 50 ° C, stirred and dissolved to prepare a complex dicarboxylic acid solution containing succinic acid, glutaric acid, and adipic acid at concentrations of 1.02 mol / Kg, 2.20 mol / Kg, and 0.34 mol / Kg, respectively. did. Then, this solution was allowed to stand at room temperature with an acrylic strong base anion exchange resin (Amberlite IRA-45, manufactured by Organo).
8) was passed through a column packed with 8) with a SV ratio of 10 and subsequently with a column packed with polystyrene sulfonic acid type strong acid cation exchange resin (Amberlite IR-124, manufactured by Olgano) at an SV ratio of 5 to form a composite. After removing heavy metals in the dicarboxylic acid solution (the total concentration of Fe, Cu, Ni, Mn, Zn, Cr in the treatment solution is 0.6 mg / Kg
Each of the solutions, Cu, Mn, and Zn was 0.04 mg / Kg or less), 100 parts by weight of a 12.6 wt% hydrogen peroxide aqueous solution to 100 parts by weight of this solution, and 1-hydroxyethylidene-1,1 as a stabilizer. -Mixed with 60% by weight aqueous solution of diphosphonic acid 0.50 parts by weight, the initial concentrations of succinic acid, glutaric acid, adipic acid and hydrogen peroxide were 0.51 mol / Kg and 1.10, respectively.
Mol / Kg, 0.16 mol / Kg and 1.85 mol / Kg, and a stabilizer (pure content) of 0.15% by weight at 50 ° C
The reaction was carried out for 72 hours while heating and stirring. The solution after the reaction contained 0.18 mol / Kg of perdicarboxylic acid, 1.59 mol / Kg of dicarboxylic acid excluding perdicarboxylic acid, and 1.66 mol / Kg of hydrogen peroxide. The concentrations of succinic acid (including persuccinic acid), adipic acid (including peradipic acid), and glutaric acid (including perglutaric acid) in this solution are the same as the initial concentration. The molar ratio of the dicarboxylic acid was 0.61. When this solution was stored at 0 to 3 ° C for 4 days, precipitation of crystals was not observed, and the residual ratio of the peroxide component when stored at 50 ° C for 7 days was 97.9%.

【0033】比較例5 粗ジカルボン酸を水に溶解して調製した重金属Fe,Cu,N
i,Mn,Zn,Crの総濃度が2.8mg/Kgで含有する複合ジカル
ボン酸溶液について、陽イオン交換樹脂による重金属の
除去処理を行わなかった以外は実施例5と同様の反応を
行った。反応後の溶液は過ジカルボン酸を 0.25モル/K
gの濃度でしか含有しなかった。
Comparative Example 5 Heavy metal Fe, Cu, N prepared by dissolving a crude dicarboxylic acid in water
With respect to the composite dicarboxylic acid solution containing the total concentration of i, Mn, Zn and Cr at 2.8 mg / Kg, the same reaction as in Example 5 was carried out except that the heavy metal removal treatment with the cation exchange resin was not carried out. After the reaction, the solution contains 0.25 mol / K of perdicarboxylic acid.
It was contained only at a concentration of g.

【0034】実施例7 コハク酸、グルタル酸、アジピン酸がそれぞれ 25重量
%、64重量%、11重量%の割合で含有される粗ジカルボ
ン酸を原料とし、この1.1重量部に水1重量部を加え、50
℃に加温し、攪拌溶解させ、コハク酸、グルタル酸、ア
ジピン酸がそれぞれ 1.02モル/Kg、2.20モル/Kg、0.3
4モル/Kgの濃度で含有する複合ジカルボン酸溶液を調
製した。次いでこの溶液を室温下、ポリスチレンスルホ
ン酸型強酸性陽イオン交換樹脂(オルカ゛ノ製,アンハ゛ーライト200
C)を充填したカラムにSV比5で通液し、複合ジカルボ
ン酸溶液中の重金属を除去した後、この溶液100重量部
に対し60重量%過酸化水素を200重量部、98重量%濃硫
酸 2重量部、安定剤として1-ヒドロキシエチリデン-1,1
-ジホスホン酸 60重量%水溶液 1重量部及びジピコリン
酸0.5重量部を混合し、50℃に加温下、攪拌を行いつつ
3時間反応を行った。この反応溶液100重量部に対し水4
0重量部を加え、過ジカルボン酸を0.61モル/Kg、過ジ
カルボン酸を除いたジカルボン酸が0.23モル/Kg、過酸
化水素が7.67モル/Kgの割合で含有する溶液とし、この
溶液を50℃で貯蔵することで24時間後に成分組成がそれ
ぞれ順に0.45モル/Kg、0.39モル/Kg、7.81モル/Kgに
変化した平衡組成液を得た。平衡組成液の50℃,7日間
貯蔵に於ける過酸化物成分残存率は98.8%の値であり、
液中のコハク酸(過コハク酸を含む)、グルタル酸(過
グルタル酸を含む)、アジピン酸(過アジピン酸を含
む)の各濃度はそれぞれ0.24モル/Kg、0.51モル/Kg、
0.08モル/Kg、グルタル酸に対するその他のジカルボン
酸のモル比は 0.63であった。また、この溶液を0〜3
℃の低温で4日間貯蔵したが結晶の析出は観察されなか
った。
Example 7 A crude dicarboxylic acid containing succinic acid, glutaric acid, and adipic acid in the proportions of 25% by weight, 64% by weight, and 11% by weight, respectively, was used as a raw material. In addition, 50
Heat to ℃, stir to dissolve, succinic acid, glutaric acid, adipic acid 1.02mol / Kg, 2.20mol / Kg, 0.3
A complex dicarboxylic acid solution containing 4 mol / Kg was prepared. Then, this solution was allowed to stand at room temperature with polystyrene sulfonic acid type strong acid cation exchange resin (manufactured by Organo, Amberlite 200).
After passing through the column filled with C) at an SV ratio of 5 to remove heavy metals in the complex dicarboxylic acid solution, 200 parts by weight of 60% by weight hydrogen peroxide and 98% by weight concentrated sulfuric acid are added to 100 parts by weight of this solution. 2 parts by weight, 1-hydroxyethylidene-1,1 as a stabilizer
-1 part by weight of a 60% by weight aqueous solution of diphosphonic acid and 0.5 part by weight of dipicolinic acid were mixed, and the reaction was carried out for 3 hours while heating and stirring at 50 ° C. 4 parts of water to 100 parts by weight of this reaction solution
0 parts by weight was added to make a solution containing 0.61 mol / Kg of perdicarboxylic acid, 0.23 mol / Kg of dicarboxylic acid excluding perdicarboxylic acid, and 7.67 mol / Kg of hydrogen peroxide. After storage for 24 hours, an equilibrium composition liquid was obtained in which the component compositions were changed to 0.45 mol / Kg, 0.39 mol / Kg, and 7.81 mol / Kg, respectively. When the equilibrium composition liquid is stored at 50 ° C for 7 days, the residual ratio of peroxide component is 98.8%,
The concentrations of succinic acid (including persuccinic acid), glutaric acid (including perglutaric acid), and adipic acid (including peradipic acid) in the liquid are 0.24 mol / Kg and 0.51 mol / Kg, respectively.
The molar ratio of other dicarboxylic acid to glutaric acid was 0.08 mol / Kg, and was 0.63. In addition, this solution 0-3
It was stored at a low temperature of ° C for 4 days, but no precipitation of crystals was observed.

【0035】実施例8 コハク酸、グルタル酸、アジピン酸がそれぞれ 25重量
%、64重量%、11重量%の割合で含有される粗ジカルボ
ン酸を原料とし、この1.1重量部に水1重量部を加え、50
℃に加温し、攪拌溶解させ、コハク酸、グルタル酸、ア
ジピン酸がそれぞれ 1.02モル/Kg、2.20モル/Kg、0.3
4モル/Kgの濃度で含有する複合ジカルボン酸溶液を調
製した。次いでこの溶液を室温下、ポリスチレンスルホ
ン酸型強酸性陽イオン交換樹脂(オルカ゛ノ製,アンハ゛ーライト200
C)を充填したカラムにSV比5で通液し、複合ジカルボ
ン酸溶液中の重金属を除去した後、この溶液100重量部
に対し60重量%過酸化水素40重量部、98重量%濃硫酸 1
重量部、安定剤として1-ヒドロキシエチリデン-1,1-ジ
ホスホン酸60重量%水溶液 1重量部及びジピコリン酸0.
5重量部を加えて混合し、50℃に加温下、攪拌を行いつ
つ2時間反応させた。この溶液100重量部に水 140重量
部を加えて希釈の後、室温で放置し、1週間後に過ジカ
ルボン酸を 0.13モル/Kg、過ジカルボン酸を除いたジ
カルボン酸が0.91モル/Kg、過酸化水素が1.93モル/Kg
の割合で含有する平衡組成液を得た。平衡組成液の50
℃,7日間貯蔵に於ける過酸化物成分残存率は99.1%の
値であり、液中のコハク酸(過コハク酸を含む)、グル
タル酸(過グルタル酸を含む)、アジピン酸(過アジピ
ン酸を含む)の各濃度はそれぞれ0.30モル/Kg、0.64モ
ル/Kg、0.10モル/Kg、グルタル酸に対するその他のジ
カルボン酸のモル比は 0.63であった。また、この溶液
を0〜3℃の低温で4日間貯蔵したが結晶の析出は観察
されなかった。
Example 8 A crude dicarboxylic acid containing succinic acid, glutaric acid and adipic acid in the proportions of 25% by weight, 64% by weight and 11% by weight, respectively, was used as a raw material. In addition, 50
Heat to ℃, stir to dissolve, succinic acid, glutaric acid, adipic acid 1.02mol / Kg, 2.20mol / Kg, 0.3
A complex dicarboxylic acid solution containing 4 mol / Kg was prepared. Then, this solution was allowed to stand at room temperature with polystyrene sulfonic acid type strong acid cation exchange resin (manufactured by Organo, Amberlite 200).
After passing through the column filled with C) at an SV ratio of 5 to remove the heavy metals in the complex dicarboxylic acid solution, 60 parts by weight of hydrogen peroxide 40 parts by weight and 98% by weight concentrated sulfuric acid 1 to 100 parts by weight of this solution 1
Parts by weight, 1 part by weight of a 60% by weight aqueous solution of 1-hydroxyethylidene-1,1-diphosphonic acid as a stabilizer and 0.
5 parts by weight were added and mixed, and the mixture was reacted for 2 hours while being heated to 50 ° C. with stirring. After diluting 100 parts by weight of this solution with 140 parts by weight of water, the mixture was allowed to stand at room temperature, and after 1 week, 0.13 mol / Kg of perdicarboxylic acid, 0.91 mol / Kg of dicarboxylic acid excluding perdicarboxylic acid and peroxide were added. Hydrogen is 1.93 mol / Kg
An equilibrium composition liquid containing it in the proportion of was obtained. 50 of equilibrium composition liquid
The residual rate of peroxide components after storage at 7 ℃ for 7 days was 99.1%, and succinic acid (including persuccinic acid), glutaric acid (including perglutaric acid), adipic acid (peradipine) Acid (including acid) was 0.30 mol / Kg, 0.64 mol / Kg, 0.10 mol / Kg, and the molar ratio of other dicarboxylic acid to glutaric acid was 0.63. Further, this solution was stored at a low temperature of 0 to 3 ° C. for 4 days, but no precipitation of crystals was observed.

【0036】実施例9及び比較例6 実施例1、4及び5で得られた過ジカルボン酸含有水溶
液と比較例4で得られた水溶液について下記の方法で殺
菌作用の試験を行い、その結果を表3に示した。 〔試験方法〕試験原液として下水処理場汚水を用い、こ
の一定量に、過ジカルボン酸含有水溶液を過ジカルボン
酸濃度が所定の濃度となる様に添加し、室温で60分間
攪拌接触させた溶液中の大腸菌数を、下水試験方法(下
水道法)の大腸菌群(デスオキシコール酸塩培地による
平板培養法)に準じて算出し、また、試験原液について
過ジカルボン酸含有水溶液を添加することなく同一方法
で原液中の大腸菌数を算出し、過ジカルボン酸含有水溶
液による殺菌効果を次の計算式で求めた生存率値として
表示した。 生存率=(過ジカルボン酸含有水溶液添加処理液中の菌
数)×100/(原液中の菌数) 複合ジカルボン酸からの過ジカルボン酸含有水溶液はグ
ルタル酸のみから誘導された過ジカルボン酸含有水溶液
よりも過ジカルボン酸モル当たりの殺菌作用が良好であ
った。
Example 9 and Comparative Example 6 The perdicarboxylic acid-containing aqueous solution obtained in Examples 1, 4 and 5 and the aqueous solution obtained in Comparative Example 4 were tested for bactericidal action by the following method, and the results are shown. The results are shown in Table 3. [Test method] Sewage treatment plant sewage was used as a test stock solution, and a perdicarboxylic acid-containing aqueous solution was added to this fixed amount so that the perdicarboxylic acid concentration became a predetermined concentration, and the mixture was stirred and contacted at room temperature for 60 minutes. The number of Escherichia coli was calculated according to the coliform group (plate culture method using desoxycholate medium) of the sewage test method (sewerage method), and the same method was used for the test stock solution without adding the perdicarboxylic acid-containing aqueous solution. The number of Escherichia coli in the stock solution was calculated with, and the bactericidal effect of the aqueous solution containing perdicarboxylic acid was displayed as the survival rate value calculated by the following calculation formula. Survival rate = (number of bacteria in treatment solution containing perdicarboxylic acid-containing aqueous solution) x 100 / (number of bacteria in undiluted solution) Perdicarboxylic acid-containing aqueous solution from complex dicarboxylic acid is a perdicarboxylic-acid-containing aqueous solution derived from glutaric acid only The bactericidal action per mol of perdicarboxylic acid was better than that.

【0037】[0037]

【表3】 [Table 3]

【0038】実施例10及び比較例7 実施例6で調製した過ジカルボン酸含有水溶液とグルタ
ル酸のみから調製した過ジカルボン酸含有水溶液を使用
し、下記の方法で大腸菌に対する最小殺菌濃度の測定を
行った。その結果は表4に示した様に、本発明による過
ジカルボン酸含有水溶液がグルタル酸のみから誘導され
た過ジカルボン酸含有水溶液よりも低い濃度で殺菌作用
を示した。 〔試験方法〕過ジカルボン酸含有水溶液を蒸留水で希釈
し、過ジカルボン酸濃度が所定の濃度になるように希釈
試験液10mlに、菌数約107個/mlに調整した増殖大腸菌
液0.1mlを添加し、30分間接触させた後、その0.1mlを
ブレインハートインフュージョン培地10mlに接種し、37
℃で48時間培養し、濁り発生の有無から大腸菌増殖の有
無を判定した。
Example 10 and Comparative Example 7 Using the perdicarboxylic acid-containing aqueous solution prepared in Example 6 and the perdicarboxylic acid-containing aqueous solution prepared only from glutaric acid, the minimum bactericidal concentration against E. coli was measured by the following method. It was As a result, as shown in Table 4, the perdicarboxylic acid-containing aqueous solution according to the present invention exhibited a bactericidal action at a lower concentration than the perdicarboxylic acid-containing aqueous solution derived from glutaric acid alone. [Test method] Dilute the perdicarboxylic acid-containing aqueous solution with distilled water and adjust the perdicarboxylic acid concentration to a predetermined concentration in 10 ml of diluted test solution and 0.1 ml of proliferating Escherichia coli solution adjusted to about 10 7 cells / ml. Was added, and after contacting for 30 minutes, 0.1 ml of the mixture was inoculated into 10 ml of Brain Heart Infusion Medium, 37
The cells were cultured at ℃ for 48 hours, and the presence or absence of E. coli growth was determined based on the presence or absence of turbidity.

【0039】[0039]

【表4】 [Table 4]

【0040】実施例11及び比較例8 実施例6で調製した過ジカルボン酸含有水溶液とグルタ
ル酸のみから調製した過ジカルボン酸含有水溶液を使用
し、これらを水で希釈するとともにpHを調製した漂白
液について下記の方法で漂白作用の試験を行い、その結
果を表5に示した。
Example 11 and Comparative Example 8 A bleaching solution prepared by using the aqueous solution containing perdicarboxylic acid prepared in Example 6 and the aqueous solution containing perdicarboxylic acid prepared only from glutaric acid, and diluting these with water and adjusting the pH. Was tested for bleaching action by the following method, and the results are shown in Table 5.

【0041】〔漂白試験〕過ジカルボン酸含有水溶液の
所定量に水道水を加えて希釈するとともに水酸化ナトリ
ウム水溶液を加えてpHを所定値に調製し、表5に示し
た過カルボン酸濃度、pHを有する漂白液を調整し
た。、汚染布重量の50倍量の漂白液量を使用し、これ
に紅茶汚染布を浸漬して40℃で30分間の漂白を行った。
漂白後の布は水洗、乾燥、アイロン掛けを行った後、
色差計によって反射率を測定し、次式から漂白率を算出
した。 漂白率(%)=(B−A)×100/(C−A),ここで
Aは漂白前汚染布の反射率を、Bは漂白後汚染布の反射
率を、Cは紅茶汚染前白布の反射率を表す。
[Bleaching test] Tap water was added to a predetermined amount of the perdicarboxylic acid-containing aqueous solution to dilute it, and an aqueous sodium hydroxide solution was added to adjust the pH to a predetermined value. A bleaching solution having A bleaching solution amount of 50 times the weight of the contaminated cloth was used, and the tea contaminated cloth was immersed in the bleaching solution and bleached at 40 ° C. for 30 minutes.
After the bleached cloth is washed with water, dried and ironed,
The reflectance was measured with a color difference meter, and the bleaching rate was calculated from the following formula. Bleaching rate (%) = (B−A) × 100 / (C−A), where A is the reflectance of the stained cloth before bleaching, B is the reflectance of the stained cloth after bleaching, and C is the white cloth before staining with black tea. Represents the reflectance.

【0042】[0042]

【表5】 [Table 5]

───────────────────────────────────────────────────── フロントページの続き (51)Int.Cl.6 識別記号 庁内整理番号 FI 技術表示箇所 C11D 7/38 ─────────────────────────────────────────────────── ─── Continuation of the front page (51) Int.Cl. 6 Identification code Office reference number FI technical display location C11D 7/38

Claims (3)

【特許請求の範囲】[Claims] 【請求項1】 グルタル酸とコハク酸とを含む複合ジカ
ルボン酸と過酸化水素とを反応させて得られる、 (1)過ジカルボン酸(モノ過ジカルボン酸換算)が
0.05 〜 1.0 モル/Kg溶液、 (2)過ジカルボン酸を除く総ジカルボン酸類が 0.2
〜 2.2モル/Kg溶液、 (3)過酸化水素が 1.0 〜 12.0 モル/Kg溶液、 (4)安定剤が 0.01〜3.0重量%の濃度で含有され、か
つコハク酸(過コハク酸を含む)濃度が 0.1 〜 0.7モ
ル/Kg溶液の範囲で、またグルタル酸(過グルタル酸を
含む)1モルに対するコハク酸(過コハク酸を含む)の
モル比率が0.1〜2.0の割合で含有される過ジカルボン酸
含有水溶液。
1. A (1) perdicarboxylic acid (converted to monoperdicarboxylic acid) obtained by reacting a complex dicarboxylic acid containing glutaric acid and succinic acid with hydrogen peroxide.
0.05 to 1.0 mol / Kg solution, (2) 0.2% total dicarboxylic acids except perdicarboxylic acid
~ 2.2 mol / Kg solution, (3) Hydrogen peroxide is 1.0 ~ 12.0 mol / Kg solution, (4) Stabilizer is contained at a concentration of 0.01 ~ 3.0 wt%, and succinic acid (including persuccinic acid) concentration Is in the range of 0.1-0.7 mol / Kg solution, and the molar ratio of succinic acid (including persuccinic acid) to 1 mol of glutaric acid (including perglutaric acid) is 0.1-2.0. Containing aqueous solution.
【請求項2】 グルタル酸とコハク酸及びアジピン酸を
含む複合ジカルボン酸と過酸化水素とを反応させて得ら
れる、 (1)過ジカルボン酸(モノ過ジカルボン酸換算)が
0.05 〜 1.0 モル/Kg溶液、 (2)過ジカルボン酸を除く総ジカルボン酸類が 0.2
〜 2.2モル/Kg溶液、 (3)過酸化水素が 1.0 〜 12.0 モル/Kg溶液、 (4)安定剤が 0.01〜3.0重量%の濃度で含有され、か
つコハク酸(過コハク酸を含む)濃度が 0.1 〜 0.7モ
ル/Kg溶液、アジピン酸(過アジピン酸を含む)濃度が
0.02〜0.2モル/Kg溶液の範囲で、またグルタル酸(過
グルタル酸を含む)1モルに対するその他ジカルボン酸
(それぞれの過ジカルボン酸を含む)合計のモル比率が
0.1〜2.0の割合で含有される過ジカルボン酸含有水溶
液。
2. A (1) perdicarboxylic acid (converted to a monoperdicarboxylic acid) obtained by reacting a complex dicarboxylic acid containing glutaric acid, succinic acid and adipic acid with hydrogen peroxide.
0.05 to 1.0 mol / Kg solution, (2) 0.2% total dicarboxylic acids except perdicarboxylic acid
~ 2.2 mol / Kg solution, (3) Hydrogen peroxide is 1.0 ~ 12.0 mol / Kg solution, (4) Stabilizer is contained at a concentration of 0.01 ~ 3.0 wt%, and succinic acid (including persuccinic acid) concentration 0.1-0.7 mol / Kg solution, adipic acid (including peradipic acid) concentration
In the range of 0.02 to 0.2 mol / Kg solution, the total molar ratio of other dicarboxylic acids (including each perdicarboxylic acid) to 1 mol of glutaric acid (including perglutaric acid) is
A perdicarboxylic acid-containing aqueous solution that is contained at a ratio of 0.1 to 2.0.
【請求項3】 ジカルボン酸類を水に溶解した複合ジカ
ルボン酸水溶液をイオン交換樹脂あるいはキレート樹脂
で処理し、含有する 鉄、銅、ニッケル、クロム、マン
ガン、亜鉛の総金属濃度を 2.0mg/kg以下とした複合ジ
カルボン酸水溶液を用い、安定剤の共存下に過酸化水素
と反応させることを特徴とする請求項1〜2に記載の過
ジカルボン酸含有水溶液の製造方法。
3. A composite dicarboxylic acid aqueous solution in which dicarboxylic acids are dissolved in water is treated with an ion exchange resin or a chelate resin, and the total metal concentration of iron, copper, nickel, chromium, manganese, and zinc contained is 2.0 mg / kg or less. The method for producing a perdicarboxylic acid-containing aqueous solution according to claim 1, wherein the complex dicarboxylic acid aqueous solution described above is reacted with hydrogen peroxide in the presence of a stabilizer.
JP14413695A 1994-06-22 1995-05-19 Aqueous solution containing perdicarboxylic acid Expired - Fee Related JP3537540B2 (en)

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Publication number Priority date Publication date Assignee Title
WO1997028691A1 (en) * 1996-02-12 1997-08-14 Healthpoint, Ltd. Quick acting chemical sterilant
WO2006068306A2 (en) 2004-12-22 2006-06-29 Fujifilm Corporation COMPOSITION FOR STERILIZATION COMPRISING ω-ALKOXYPEROXYCARBOXYLIC ACID
WO2007035987A1 (en) 2005-09-27 2007-04-05 Siemens Water Technologies Corp. Chemical cleaning agent and process for cleaning filtration membranes
WO2007102389A1 (en) * 2006-03-08 2007-09-13 Mitsubishi Gas Chemical Company, Inc. Process for producing dilute perglutaric acid solution
JP2010184869A (en) * 2009-02-10 2010-08-26 Mitsubishi Gas Chemical Co Inc Method for producing persuccinate-containing composition
CN103145228A (en) * 2013-03-06 2013-06-12 青岛大学 Method for decoloring wastewater dyed by active dye

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* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JP4984578B2 (en) * 2006-03-08 2012-07-25 三菱瓦斯化学株式会社 Method for producing stable organic peracid polymer composition

Cited By (7)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
WO1997028691A1 (en) * 1996-02-12 1997-08-14 Healthpoint, Ltd. Quick acting chemical sterilant
CN1084149C (en) * 1996-02-12 2002-05-08 海尔斯波因特有限公司 Quick acting chemical sterilant
WO2006068306A2 (en) 2004-12-22 2006-06-29 Fujifilm Corporation COMPOSITION FOR STERILIZATION COMPRISING ω-ALKOXYPEROXYCARBOXYLIC ACID
WO2007035987A1 (en) 2005-09-27 2007-04-05 Siemens Water Technologies Corp. Chemical cleaning agent and process for cleaning filtration membranes
WO2007102389A1 (en) * 2006-03-08 2007-09-13 Mitsubishi Gas Chemical Company, Inc. Process for producing dilute perglutaric acid solution
JP2010184869A (en) * 2009-02-10 2010-08-26 Mitsubishi Gas Chemical Co Inc Method for producing persuccinate-containing composition
CN103145228A (en) * 2013-03-06 2013-06-12 青岛大学 Method for decoloring wastewater dyed by active dye

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