JP3537540B2 - Aqueous solution containing perdicarboxylic acid - Google Patents

Aqueous solution containing perdicarboxylic acid

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Publication number
JP3537540B2
JP3537540B2 JP14413695A JP14413695A JP3537540B2 JP 3537540 B2 JP3537540 B2 JP 3537540B2 JP 14413695 A JP14413695 A JP 14413695A JP 14413695 A JP14413695 A JP 14413695A JP 3537540 B2 JP3537540 B2 JP 3537540B2
Authority
JP
Japan
Prior art keywords
acid
mol
solution
concentration
perdicarboxylic
Prior art date
Legal status (The legal status is an assumption and is not a legal conclusion. Google has not performed a legal analysis and makes no representation as to the accuracy of the status listed.)
Expired - Fee Related
Application number
JP14413695A
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Japanese (ja)
Other versions
JPH0867667A (en
Inventor
律雄 阿部
新平 橋本
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
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Priority to JP14413695A priority Critical patent/JP3537540B2/en
Publication of JPH0867667A publication Critical patent/JPH0867667A/en
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Anticipated expiration legal-status Critical
Expired - Fee Related legal-status Critical Current

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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 aqueous solution of a perdicarboxylic acid for use in applications such as sterilization, bleaching and washing, and a process 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。
2. Description of the Related Art Percarboxylic acids are usually synthesized from carboxylic acid or carboxylic anhydride and hydrogen peroxide, and are widely used as oxidizing agents for various substances due to their oxidizing power. It is also used in these applications because it exhibits such effects as the above. Use forms of these peracids are roughly classified into solid forms and aqueous forms. Peracetic acid is known as a typical aqueous carboxylic acid. Peracetic acid has its stability,
Alternatively, it is widely used for sterilization, bleaching, washing, etc. due to the generality of acetic acid as a raw material, but depending on the application, its use may be restricted by the peculiar smell of peracetic acid, which solves this problem. For this reason, various stable and odorless peracids have been studied, and JP-A-53-81619 proposes an odorless and stable perglutaric acid concentrated solution.

【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。
[0003] Other odorless peracids include perdicarboxylic acids such as persuccinic acid and peradipic acid. The production of peracid is based on the carboxylic acid and hydrogen peroxide used as raw materials and the produced peracid. Since the concentration of carboxylic acid and hydrogen peroxide during the reaction is higher, the higher the concentration, the more efficiently the peracid is generated, whereas the succinic acid and adipic acid, which are the raw materials for these peracids, It is disadvantageous in terms of production efficiency because solubility is low and efficient formation of peracid is not performed.
Also, since only a low concentration of peracid solution can be obtained, it is disadvantageous in distribution and the like. For the production of these peracids, acid anhydrides such as succinic anhydride or adipic anhydride are mainly used. Is used as a raw material.

【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。
[0004] However, aqueous solutions of peracid derived from these anhydrides can generate high concentrations of peracid, but as the peracid decomposes, hardly soluble host acid crystals are precipitated when cooled. It has problems from the viewpoints of stability and safety over time and safety, and also has the economic reason that the raw material anhydride is relatively expensive. Is almost never 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。
[0005] 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 they are scarce and expensive, general use is more difficult in terms of raw material availability and economics.

【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。
SUMMARY OF THE INVENTION It is an object of the present invention to provide a method for producing a perdicarboxylic acid-containing aqueous solution derived from such an odorless, low-solubility dicarboxylic acid, which is disadvantageous due to a change with time, or a disadvantage in production efficiency and distribution. For general sterilization, bleaching, and washing with excellent stability or performance and economic efficiency, which has improved the effect and economical issues 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 The present inventors have conducted intensive studies on these problems and as a result, mixed water-soluble glutaric acid with succinic acid and adipic acid having low water solubility,
The aqueous solution of the complex dicarboxylic acid in which these odorless dicarboxylic acids are dissolved can dissolve succinic acid and adipic acid having low water solubility at a higher concentration in the existing water, and the aqueous solution of the complex dicarboxylic acid can be dissolved in the aqueous solution of the complex dicarboxylic acid. By adding and reacting with hydrogen oxide, the perdicarboxylic acid is efficiently formed even when the use ratio of glutaric acid is reduced, which can improve economical problems, and the resulting specific concentration composition can be improved. The dicarboxylic acid-containing aqueous solution was found to be excellent in the effect of its use, and it was difficult to cause crystal precipitation during storage, thereby improving the problems of the odorless perdicarboxylic acid-containing aqueous solution derived from a single dicarboxylic acid. It is found that an aqueous solution containing perdicarboxylic acid can be obtained which is more excellent in 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。
[0008] That is, the present invention provides a dicarboxylic acid containing glutaric acid and succinic acid, which is obtained by reacting hydrogen peroxide with (1) a percarboxylic acid (in terms of monopercarboxylic acid) of 0.05 to 1.0 mol. / Kg solution, (2) 0.2 to 2.2 mol / Kg of total dicarboxylic acids excluding perdicarboxylic acid
Solution, (3) a hydrogen peroxide solution of 1.0 to 12.0 mol / Kg,
(4) The stabilizer is contained at a concentration of 0.01 to 3.0% by weight,
And a succinic acid (including persuccinic acid) concentration of 0.1 to 0.7
Succinic acid (including persuccinic acid) per mole of glutaric acid (including perglutaric acid) in the range of mol / Kg solution
(1) a percarboxylic acid-containing aqueous solution containing a molar ratio of 0.1 to 2.0, and a complex dicarboxylic acid containing succinic acid and adipic acid and hydrogen peroxide reacted with hydrogen peroxide. 0.05 to 1.0 mol / Kg solution of dicarboxylic acid (in terms of monoperdicarboxylic acid), (2) 0.2 to 2.2 mol / Kg of total dicarboxylic acids excluding perdicarboxylic acid
Solution, (3) a hydrogen peroxide solution of 1.0 to 12.0 mol / Kg,
(4) The stabilizer is contained at a concentration of 0.01 to 3.0% by weight, and 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 respective perdicarboxylic acids) to 1 mol of glutaric acid (including perglutaric acid) is as follows.
The present invention relates to a perdicarboxylic acid-containing aqueous solution contained at 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 aqueous solution containing perdicarboxylic acid of the present invention contains glutaric acid as an essential component, uses succinic acid and adipic acid in combination, and dissolves these dicarboxylic acids in water to obtain a predetermined concentration and ratio of dicarboxylic acid. Aqueous solution, the aqueous solution is further processed and purified by an ion exchange resin or the like,
After removing the heavy metals contained, a hydrogen peroxide solution is added in the co-presence of a stabilizer, and the mixture is reacted to prepare the solution. However, if necessary, the solution can be further diluted with deionized water to a desired concentration. .

【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 aqueous solution of the complex dicarboxylic acid used in the present invention basically uses 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 in water at a ratio, but crude dicarboxylic acids in the form of a mixture of these dicarboxylic acids in a fixed ratio or a non-constant ratio are easily available, and industrially, these are used as raw materials to form a composite. It is advantageous to prepare an aqueous dicarboxylic acid solution. In this case, once dissolved in water and then cooled, the unnecessary portion of the low-soluble dicarboxylic acid is crystallized and separated and removed, or a mixed dicarboxylic acid is suspended in water to dissolve the insoluble portion. The concentration or ratio of each dicarboxylic acid is adjusted by a method of separating and removing the dicarboxylic acid or a method of mixing and using a mixed dicarboxylic acid and a single dicarboxylic acid to prepare a desired aqueous solution of a complex dicarboxylic acid. In addition, if particularly desired, anhydrides of these dicarboxylic acids can be used, and they can be dissolved in water and hydrated.

【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 solubility of low-solubility dicarboxylic acids such as succinic acid or adipic acid in water increases as shown in Table 1 due to the coexistence of glutaric acid, whereby the amount of low-solubility dicarboxylic acids present in the aqueous solution of complex dicarboxylic acid increases. Since the dissolution ratio can be increased and more dicarboxylic acids can be dissolved in less water, the reaction of perdicarboxylic acid, which is an equilibrium reaction, can be performed 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 dicarboxylic acid in the aqueous solution of complex dicarboxylic acid is related to the composition of the final aqueous solution containing percarboxylic acid, and the ratio of hydrogen peroxide to dicarboxylic acid added during the reaction or the amount of hydrogen peroxide used is Since the concentration or the like is selected, it cannot be specified unconditionally, but in general, the operability of purification operation of the aqueous solution of dicarboxylic acid with an ion exchange resin or a chelate resin, the removal efficiency of heavy metals, or the intended excess From the efficiency of dicarboxylic acid formation, the solution is subjected to treatment with an ion exchange resin as a 2 to 6 mol / Kg solution, preferably 3 to 5 mol / Kg solution as a dicarboxylic acid concentration.

【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 used as a raw material usually contains a trace amount of heavy metal as an impurity, and coexists during the reaction between the dicarboxylic acid and hydrogen peroxide, thereby inhibiting the formation of the dicarboxylic acid, and If the concentration of perdicarboxylic acid is not obtained, or if it is present in the final perdicarboxylic acid-containing aqueous solution, the decomposition of perdicarboxylic acid or hydrogen peroxide is promoted, and the storage stability is reduced.
In order to cause practical problems, for the purpose of removing these metal ions, dicarboxylic acids are converted to an aqueous solution and then treated with an ion exchange resin or a chelate resin, and iron, copper, nickel, chromium, Reduce the total heavy metal ion concentration of manganese and zinc to 2 mg / Kg solution or less. As the ion exchange resin here, a generally known strong acidic cation exchange resin having a sulfonic acid group as an ion exchange functional group can be suitably used, and the chelate resin has an iminodiacetic acid group, or Further, a polyamine type generally known chelate resin can be used. The removal of metals in the aqueous solution of dicarboxylic acid can be carried out with a cation exchange resin or a chelate resin to roughly remove the target metal. If stabilization is desired, an even better storage stability can be obtained by further using an anion exchange resin before the treatment with the cation exchange resin to remove trace metals 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。
The treatment of the raw material dicarboxylic acid aqueous solution with an ion exchange resin or a chelate resin may be carried out by a general method such as a method of suspending the resin in the aqueous solution of dicarboxylic acid and separating by filtration, or a method of passing 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 at the time of treatment, the concentration of the dicarboxylic acid in the treatment solution is set to be equal to or less than the saturation concentration at the treatment temperature, and the concentration of the heavy metals is 2.0 mg / kg. Hereinafter, it is desirably provided 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 regenerated with an aqueous solution of a mineral acid such as dilute sulfuric acid and recycled.

【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:
A mixed dicarboxylic acid aqueous solution purified by the above method and a hydrogen peroxide aqueous solution are mixed in the presence of a stabilizer, and the mixture is reacted under stirring.If desired, deionized water is added during the reaction. 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 of 0 to 30 ° C. for a long time, but it is not efficient for industrial production.
To 80 ° C., preferably 40 to 60 ° C., and if necessary, if necessary, a reaction solution using an acidic substance such as sulfuric acid, phosphoric acid, condensed phosphoric acid, or phosphonic acid as a catalyst. The reaction time can be further reduced 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 during the reaction, it is necessary that the reaction solution is highly stabilized. If the raw material dicarboxylic acid aqueous solution is insufficiently purified, or if the amount of the stabilizer is small, If it is not enough,
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,
The reaction is preferably carried out for 4 to 50 hours.However, when the final concentration of perdicarboxylic acid is low, such as when the reaction solution is diluted to a final composition after the reaction, the reaction time may be reduced. As a result, it is possible to shorten the time without being restricted by the time required to reach the equilibrium composition.

【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 solution, but the dicarboxylic acid concentration in the reaction solution is kept constant. In this case, as the ratio of hydrogen peroxide to dicarboxylic acid increases, the ratio or concentration of generated perdicarboxylic acid increases, and although it is efficient in terms of perdicarboxylic acid generation, the concentration of hydrogen peroxide is simultaneously increased. Therefore, it is not preferable to use an excessively large amount because the increase in the peroxide concentration increases the potential danger in handling or storing the final composition liquid. Also, it is not efficient to use a ratio lower than necessary in that the production rate of perdicarboxylic acid is reduced,
In the present invention, the molar ratio of hydrogen peroxide to dicarboxylic acid is from 0.2 to 15, preferably from 0.5 to 10. The concentration of hydrogen peroxide to be used is usually 10 to 70% by weight from the viewpoint of handling or danger, but when a high concentration of perdicarboxylic acid is desired to be produced, the concentration of hydrogen peroxide may be reduced 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 stabilizers added during the reaction include:
Organic phosphonic acids such as aminotri (methylenephosphonic acid), 1-hydroxyethylidene-1,1-diphosphonic acid, ethylenediaminetetra (methylenephosphonic acid) and pyridinecarboxylic acids such as picolinic acid, dipicolinic acid and quinolinic acid. Suitable and 0.01 to the reaction mixture.
The reaction is carried out by adding at a ratio of .about.3.0 wt%, preferably 0.05-1.0 wt%.

【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 aqueous solution containing perdicarboxylic acid obtained by the reaction is used as it is as a final composition solution or, if desired, water or dicarboxylic acids from which heavy metals have been removed are added.
An aqueous solution within a predetermined concentration range. The aqueous solution of percarboxylic acid containing dicarboxylic acids, hydrogen peroxide,
The composition of water eventually changes to its equilibrium composition, and the higher the concentration of dicarboxylic acids, the higher the concentration of perdicarboxylic acid is allowed, but if it is higher than necessary, crystals will precipitate when cooled. Etc. are likely to occur,
If the concentration is too low, the concentration of the dicarboxylic acid will be unnecessarily lowered, so that the dicarboxylic acids except for the dicarboxylic acid are 0.2 to 2.2 mol / Kg solution, preferably 0.1 to 0.2 mol / Kg.
Make a 3-1.8 mol / Kg solution. Also, with respect to 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 and dicarboxylic acid increases, the potential danger of the aqueous solution increases, Since their use is restricted, a 1.0 to 12 mol / Kg solution as 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 contain the solution in the range of 0.05 to 1.0 mol / Kg solution, preferably in the range of 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 aqueous solution containing percarboxylic acid according to the present invention is an important factor related to the stability with time such as crystal precipitation from the aqueous solution. To avoid precipitation
Succinic acid (including persuccinic acid) concentration should be between 0.1 and
0.7 mol / kg solution, adipic acid (including peradipic acid)
The concentration should be in the range of 0.02 to 0.2 mol / Kg solution,
Further, the total molar ratio of the other dicarboxylic acids (including the respective perdicarboxylic acids) to 1 mol of the glutaric acid (including the 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。
The aqueous solution of a percarboxylic acid of the present invention may contain a surfactant, if desired, as long as the object of the present invention is not hindered.
Additives such as fragrances and coloring agents 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 comprises:
Compared to the method using only low-soluble dicarboxylic acids such as succinic acid and adipic acid, it is not only efficient in that the obtained perdicarboxylic acid concentration can be made higher, but also these low-soluble It is more practical because it has improved stability over time, such as the difficulty of precipitating crystalline dicarboxylic acid, and it is more effective than the percarboxylic acid solution obtained from glutaric acid alone. The disadvantages of each perdicarboxylic acid-containing aqueous solution derived from a single dicarboxylic acid have been 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 or 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。
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 to 50 ° C., stirred and dissolved, and succinic acid mixed with these dicarboxylic acids 0.5 to 0.8 mol / kg, adipic acid 0.1-0.3
Aqueous solution containing mol / Kg and glutaric acid at a concentration of 0.6 to 2.9 mol / Kg was prepared, and then these solutions were filled with polystyrenesulfonic acid type strongly acidic cation exchange resin (manufactured by Orcano, Amperite IR-124). The mixture was passed at 30 ° C. at an SV ratio of 4 to 6 to prepare a composite dicarboxylic acid aqueous solution having a heavy metal content of 1.0 mg / Kg solution or less. Further, a 60% by weight aqueous solution of hydrogen peroxide and a 60% by weight aqueous solution of 1-hydroxyethylidene-1,1-diphosphonic acid as a stabilizer were added to these solutions, and the initial concentrations of the respective components were set to the values shown in Table 2, and 50%. The reaction was carried out at 72 ° C for 72 hours. Table 2 shows the results of observing the concentrations of percarboxylic acid and hydrogen peroxide in the obtained reaction solution, and the presence or absence of crystal precipitation when these compositions were allowed to stand at 2-3 ° 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 0.7 mol / kg of succinic acid and 0.9 mol / kg of glutaric acid in the same manner as in Examples 1 to 3 except that succinic acid and glutaric acid were used.
After preparing an aqueous solution containing at a concentration of, and similarly treating with an ion exchange resin, adding a hydrogen peroxide solution and a stabilizer to the initial concentration 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 and 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. In addition, a 60% by weight aqueous solution of hydrogen peroxide and 1-hydroxyethylidene-1,1-
A 60% by weight aqueous solution of diphosphonic acid was added to adjust the initial concentration of each component to 0.45 mol / K for succinic acid and hydrogen peroxide, respectively.
g, 4.2 mol / Kg, and 0.56 mol / Kg, 4.5 mol / Kg were prepared and reacted in the same manner as in Examples 1 to 3 to obtain an equilibrium solution, and the resulting persuccinic acid was analyzed. Then, the solution was stored at 2-3 ° C., and the state of crystal precipitation was observed. The results are as shown in Table 2, where the concentration of percarboxylic acid produced was low, and the precipitation of crystals was observed in several days despite the fact that the total succinic acid concentration was the same or low as 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 Succinic acid was replaced with adipic acid, a solution having an adipic acid concentration of 0.18 mol / Kg was prepared, and treated in the same manner as in Comparative Example 1 to have an initial concentration of 0.13 mol / kg for adipic acid and hydrogen peroxide, respectively. A solution of Kg, 4.31 mol / Kg was prepared, and
After the reaction was carried out in the same manner as in Example 3 to obtain an equilibrium solution, the produced peradipic acid was analyzed. Then, the solution was stored at 2-3 ° C., and the state of crystal precipitation was observed. The results are as shown in Table 2, where the concentration of the produced percarboxylic acid was low, and the precipitation of crystals was observed in several days despite the low concentration of total adipic acid as in Examples 1-2. .

【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 so that 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, it was 0.11 mol / Kg as shown in Table 2.

【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 a ratio of 25% by weight, 64% by weight, and 11% by weight, respectively, was used as a raw material. The solution was cooled to 0 to 3 ° C, and the precipitated crystals were separated by filtration, and succinic acid, glutaric acid, and adipic acid were separated by 0.76 mol / Kg, respectively. A composite dicarboxylic acid solution containing 2.71 mol / Kg and 0.15 mol / Kg was prepared. Next, this solution was mixed with a polystyrenesulfonic acid-type strongly acidic cation exchange resin (manufactured by Orcano, Amperlite IR).
-124) at room temperature at an SV ratio of 5 to 8 to reduce the heavy metal content to 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 the concentration of Cu, Mn, and Zn was 0.04 mg / Kg or less, respectively, and subjected to the reaction with hydrogen peroxide. The reaction was performed with 100 parts by weight of a resin-treated complex dicarboxylic acid solution and a 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, 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)
At a concentration of 0.12% by weight while heating at 50 ° C. while stirring for 72 hours. The solution after the reaction contained 0.78 mol / Kg of dicarboxylic 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 concentrations, The molar ratio of the dicarboxylic acid was 0.35. This solution was stored at 0 to 3 ° C. for 4 days, but no precipitation of crystals was observed.
Peroxide residual ratio after storage for 95 days is 95.
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. The mixture was heated to 50 ° C and dissolved by stirring to prepare a composite 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. Next, this solution was cooled at room temperature to an acrylic strong basic anion exchange resin (manufactured by Orcano, Amperlite IRA-45).
8) was passed through a column filled with polystyrenesulfonic acid type strongly acidic cation exchange resin (manufactured by Orcano, Amperite IR-124) at an SV ratio of 5 at an SV ratio of 10 After removing heavy metals in the dicarboxylic acid solution (the total concentration of Fe, Cu, Ni, Mn, Zn, and Cr in the treatment solution is 0.6 mg / Kg
Solution, Cu, Mn, and Zn were each 0.04 mg / Kg or less), 100 parts by weight of a 12.6% by weight aqueous hydrogen peroxide solution per 100 parts by weight of this solution, and 1-hydroxyethylidene-1,1 as a stabilizer. -Mix with 0.50 parts by weight of a 60% by weight aqueous solution of diphosphonic acid, and adjust the initial concentrations of succinic acid, glutaric acid, adipic acid and hydrogen peroxide to 0.51 mol / Kg, 1.10 respectively.
Mol / Kg, 0.16 mol / Kg and 1.85 mol / Kg, and a stabilizer (pure) at a concentration of 0.15% by weight at 50 ° C.
The reaction was carried out for 72 hours while stirring while heating. The solution after the reaction contained 0.18 mol / kg of dicarboxylic 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 concentrations, The molar ratio of dicarboxylic acid was 0.61. When this solution was stored at 0 to 3 ° C for 4 days, no precipitation of crystals was 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 metals Fe, Cu, N prepared by dissolving a crude dicarboxylic acid in water
The same reaction as in Example 5 was performed for the composite dicarboxylic acid solution containing i, Mn, Zn, and Cr at a total concentration of 2.8 mg / Kg, except that the heavy metal removal treatment with the cation exchange resin was not performed. The solution after the reaction contains 0.25 mol / K of dicarboxylic acid.
Only contained 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 a ratio of 25% by weight, 64% by weight, and 11% by weight, respectively, was used. Plus 50
C. and dissolved by stirring. Succinic acid, glutaric acid and adipic acid contained 1.02 mol / Kg, 2.20 mol / Kg, 0.3
A complex dicarboxylic acid solution containing 4 mol / Kg was prepared. Then, this solution was subjected to a polystyrenesulfonic acid-type strongly acidic cation exchange resin (manufactured by Orcano, Amperlite 200) at room temperature.
The mixture was passed through a column packed with C) at an SV ratio of 5 to remove heavy metals in the composite dicarboxylic acid solution. Then, 200 parts by weight of 60% by weight hydrogen peroxide and 98% by weight of 98% by weight concentrated sulfuric acid were added to 100 parts by weight of this solution. 2 parts by weight, 1-hydroxyethylidene-1,1 as stabilizer
1 part by weight of a 60% by weight diphosphonic acid aqueous solution and 0.5 part by weight of dipicolinic acid were mixed, and the mixture was reacted at 50 ° C. for 3 hours while stirring. Water 4 per 100 parts by weight of the reaction solution
0 parts by weight were added, and a solution containing 0.61 mol / kg of dicarboxylic acid, 0.23 mol / kg of dicarboxylic acid excluding perdicarboxylic acid, and 7.67 mol / kg of hydrogen peroxide was prepared. After 24 hours, an equilibrium composition solution was obtained in which the component compositions changed to 0.45 mol / Kg, 0.39 mol / Kg, and 7.81 mol / Kg, respectively, after 24 hours. The peroxide component residual ratio of the equilibrium composition solution when stored at 50 ° C. for 7 days is 98.8%.
The concentrations of succinic acid (including persuccinic acid), glutaric acid (including perglutaric acid), and adipic acid (including peradipic acid) in the solution are 0.24 mol / Kg, 0.51 mol / Kg, respectively.
The mole ratio of other dicarboxylic acids to glutaric acid was 0.08 mol / Kg, and was 0.63. In addition, this solution is
After storage at a low temperature of 4 ° C. for 4 days, 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 at a ratio of 25% by weight, 64% by weight, and 11% by weight, respectively, was used as a raw material. Plus 50
C. and dissolved by stirring. Succinic acid, glutaric acid and adipic acid contained 1.02 mol / Kg, 2.20 mol / Kg, 0.3
A complex dicarboxylic acid solution containing 4 mol / Kg was prepared. Then, this solution was subjected to a polystyrenesulfonic acid-type strongly acidic cation exchange resin (manufactured by Orcano, Amperlite 200) at room temperature.
The mixture was passed through a column packed with C) at an SV ratio of 5 to remove heavy metals from the composite dicarboxylic acid solution. Then, 40 parts by weight of 60% by weight hydrogen peroxide and 98% by weight of concentrated sulfuric acid were added to 100 parts by weight of the solution.
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 0.1 parts by weight of dipicolinic acid.
Five parts by weight were added and mixed, and the mixture was reacted for 2 hours while stirring at a temperature of 50 ° C. After diluting 100 parts by weight of this solution with 140 parts by weight of water and leaving it at room temperature, one week later, 0.13 mol / Kg of dicarboxylic acid and 0.91 mol / Kg of dicarboxylic acid excluding perdicarboxylic acid were added. Hydrogen is 1.93 mol / Kg
Was obtained. 50 of equilibrium composition solution
Percentage of peroxide component after storage at 7 ℃ for 9 days is 99.1%. Succinic acid (including persuccinic acid), glutaric acid (including perglutaric acid), adipic acid (peradipine) (Including acid) were 0.30 mol / Kg, 0.64 mol / Kg, 0.10 mol / Kg, respectively, and the molar ratio of other dicarboxylic acids to glutaric acid was 0.63. 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 aqueous solution obtained in Examples 1, 4 and 5 and the aqueous solution obtained in Comparative Example 4 were tested for bactericidal activity by the following method. The results are shown in Table 3. [Test Method] Using a sewage treatment plant sewage as a test stock solution, a perdicarboxylic acid-containing aqueous solution was added to this fixed amount so that the perdicarboxylic acid concentration became a predetermined concentration, and the solution was stirred and contacted at room temperature for 60 minutes. Was calculated according to the coliform bacteria (plate culture method using desoxycholate medium) in the sewage test method (sewerage method), and the same method was used for the stock test solution without adding a perdicarboxylic acid-containing aqueous solution. The number of Escherichia coli in the undiluted solution was calculated, and the bactericidal effect of the perdicarboxylic acid-containing aqueous solution was displayed as a survival rate value obtained by the following formula. Viability = (the number of bacteria in the treated solution with the addition of the aqueous solution containing perdicarboxylic acid) x 100 / (the number of bacteria in the stock solution) The aqueous solution containing perdicarboxylic acid from the complex dicarboxylic acid is an aqueous solution containing perdicarboxylic acid derived only from glutaric acid The bactericidal action per mole 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 aqueous solution containing perdicarboxylic acid prepared in Example 6 and the aqueous solution containing perdicarboxylic acid prepared only from glutaric acid, the minimum bactericidal concentration against Escherichia coli was measured by the following method. Was. As shown in Table 4, the aqueous solution containing perdicarboxylic acid according to the present invention exhibited a bactericidal action at a lower concentration than the aqueous solution containing perdicarboxylic acid derived only from glutaric acid, as shown in Table 4. [Test Method] A perdicarboxylic acid-containing aqueous solution was diluted with distilled water, and 0.1 ml of a growing Escherichia coli solution adjusted to about 10 7 cells / ml in 10 ml of a diluted test solution so that the concentration of perdicarboxylic acid became a predetermined concentration. Was added and contacted for 30 minutes, and 0.1 ml of the mixture was inoculated into 10 ml of Brain Heart Infusion medium,
After culturing at 48 ° C for 48 hours, the presence or absence of Escherichia coli proliferation was determined based on the occurrence 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 The aqueous solution containing perdicarboxylic acid prepared in Example 6 and the aqueous solution containing perdicarboxylic acid prepared only from glutaric acid were used, and the bleaching solution was diluted with water and the pH was adjusted. 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 aqueous solution containing perdicarboxylic acid to dilute the solution, and an aqueous solution of sodium hydroxide was added to adjust the pH to a predetermined value. Was prepared. Using a bleaching liquid amount 50 times the weight of the stained cloth, a black tea-stained cloth was immersed in the bleaching solution and bleached at 40 ° C. for 30 minutes.
After washing, drying and ironing the bleached cloth,
The reflectance was measured by a color difference meter, and the bleaching rate was calculated from the following equation. Bleaching rate (%) = (BA) × 100 / (CA), 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 black tea staining. Represents the reflectance.

【0042】[0042]

【表5】 [Table 5]

───────────────────────────────────────────────────── フロントページの続き (51)Int.Cl.7 識別記号 FI D06L 3/02 D06L 3/02 (58)調査した分野(Int.Cl.7,DB名) C07C 409/24 A01N 37/16 C02F 1/50 532 C11D 7/38 D06L 1/12 D06L 3/02 ──────────────────────────────────────────────────の Continuing on the front page (51) Int.Cl. 7 identification code FI D06L 3/02 D06L 3/02 (58) Investigated field (Int.Cl. 7 , DB name) C07C 409/24 A01N 37/16 C02F 1/50 532 C11D 7/38 D06L 1/12 D06L 3/02

Claims (3)

(57)【特許請求の範囲】(57) [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 compound obtained by reacting a complex dicarboxylic acid containing glutaric acid and succinic acid with hydrogen peroxide, and (1) perdicarboxylic acid (in terms of monoperdicarboxylic acid)
0.05 to 1.0 mol / Kg solution, (2) 0.2% of total dicarboxylic acids excluding perdicarboxylic acid
2.22.2 mol / Kg solution, (3) 1.0-12.0 mol / Kg solution of hydrogen peroxide, (4) succinic acid (including persuccinic acid) concentration containing stabilizer at a concentration of 0.01-3.0% by weight Is in the range of 0.1 to 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 to 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 compound obtained by reacting glutaric acid, a complex dicarboxylic acid containing succinic acid and adipic acid with hydrogen peroxide, and (1) perdicarboxylic acid (in terms of monoperdicarboxylic acid)
0.05 to 1.0 mol / Kg solution, (2) 0.2% of total dicarboxylic acids excluding perdicarboxylic acid
2.22.2 mol / Kg solution, (3) 1.0-12.0 mol / Kg solution of hydrogen peroxide, (4) succinic acid (including persuccinic acid) concentration containing stabilizer at a concentration of 0.01-3.0% by weight Is 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 respective perdicarboxylic acids) to 1 mol of glutaric acid (including perglutaric acid) is as follows.
Perdicarboxylic acid-containing aqueous solution 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. An aqueous solution of a complex dicarboxylic acid obtained by dissolving dicarboxylic acids 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 aqueous solution of the complex dicarboxylic acid 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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Application Number Priority Date Filing Date Title
JP16295694 1994-06-22
JP6-162956 1994-06-22
JP14413695A JP3537540B2 (en) 1994-06-22 1995-05-19 Aqueous solution containing perdicarboxylic acid

Publications (2)

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JP3537540B2 true JP3537540B2 (en) 2004-06-14

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Cited By (1)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JP2007238776A (en) * 2006-03-08 2007-09-20 Mitsubishi Gas Chem Co Inc Method for manufacturing stable, organic peracid polymer composition

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US5827542A (en) * 1996-02-12 1998-10-27 Healthpoint, Ltd. Quick acting chemical sterilant
EP1858841B1 (en) 2004-12-22 2014-11-26 FUJIFILM Corporation Composition for sterilization comprising omega-alkoxyperoxycarboxylic acid
NZ566325A (en) 2005-09-27 2011-12-22 Siemens Water Tech Corp Chemical cleaning agent and process for cleaning filtration membranes
JPWO2007102389A1 (en) * 2006-03-08 2009-07-23 三菱瓦斯化学株式会社 Method for producing diluted perglutaric acid
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

Cited By (1)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JP2007238776A (en) * 2006-03-08 2007-09-20 Mitsubishi Gas Chem Co Inc Method for manufacturing stable, organic peracid polymer composition

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