USPatent applicationPatented

Method for generating chlorine dioxide gas, kit for generating chlorine dioxide gas, and gel composition

Granted 15 Mar 2022 · 6 office actions

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Abstract

In a method for generating a chlorine dioxide gas, the chlorine dioxide gas is continuously generated from a gel composition obtained by adding a gelling activator containing a gas generating agent, a gas generation controlling agent containing a carbonate and hydrogen peroxide, a gas generation adjusting agent, and a water-absorbent resin to a chlorite aqueous solution. This provides a method for generating a chlorine dioxide gas, a kit for generating a chlorine dioxide gas, and a gel composition which suppress the initial rapid generation of the chlorine dioxide gas and stably hold the generation of the chlorine dioxide gas for an extremely long time.

Description

20 parts
›TECHNICAL FIELD

The present invention relates to a method for generating a dilute chlorine dioxide gas used for environmental purification, sterilization or disinfection of bacteria or virus and the like, deodorization, antifungal, and antisepsis and the like of indoor (inside and outside room), outdoor or food and the like, a kit for generating a chlorine dioxide gas, and a gel composition.

›BACKGROUND ART

Chlorine dioxide has strong oxidizing power, and is widely used as a sterilization agent, a fungicide, a deodorant, a mildew-proofing agent, a preservative agent, or a bleaching agent and the like in fields such as environmental purification, sterilization or disinfection of bacteria or virus and the like, and deodorization, antifungal, and antisepsis and the like of indoor, outdoor or food and the like in house Or hospital and the like.

For the above applications, for example, Japanese Patent Laying-Open No. 11-278808 (PTL 1) discloses a pure chlorine dioxide solution having a dissolved chlorine dioxide gas, a chlorite and a pH adjuster as constituents, a gel composition containing the pure chlorine dioxide solution and a superabsorbent polymer, and continuous generation of a chlorine dioxide gas using the pure chlorine dioxide solution or the gel composition.

Japanese Patent Laying-Open No. 2003-12424 (PTL 2) discloses a chlorine dioxide composition containing a calcined aggregate, water, and dissolved chlorine dioxide in order to control the amount of a chlorine dioxide gas released, and a chlorine dioxide composition containing the chlorine dioxide composition and a gelling activator.

Japanese Patent Laying-Open No. 2005-29430 (PTL 3) discloses a method for generating a chlorine dioxide gas to further increase the generation holding time of the chlorine dioxide gas. The method includes adding organic acid or inorganic acid, a powdery gas generation adjusting agent such as sepiolite, or the gas generation adjusting agent and a water-absorbent resin to a chlorite aqueous solution to gel the chlorite aqueous solution, thereby continuously generating the chlorine dioxide gas.

›CITATION LIST

Patent Literature

PTL 1: Japanese Patent Laying-Open No. 11-278808

PTL 2: Japanese Patent Laying-Open No. 2003-12424

PTL 3: Japanese Patent Laying-Open No. 2005-29430

›SUMMARY OF INVENTION

Technical Problem

The gel composition disclosed in Japanese Patent Laying-Open No. 11-278808 (PTL 1) can continuously generate the chlorine dioxide gas for a long time, but only the addition of the superabsorbent polymer makes it difficult to adjust the transpiration rate of the chlorine dioxide gas. For example, the transpiration rate is disadvantageously increased due to an increase in a temperature.

The gel compositions disclosed in Japanese Patent Laying-Open No. 2003-12424 (PTL 2) and Japanese Patent Laying-Open No. 2005-29430 (PTL 3) can further increase the generation holding time of the chlorine dioxide gas as compared with the gel composition disclosed in Japanese Patent Application Laid-Open No. 11-278808 (PTL 1), but the amount of the chlorine dioxide gas generated is initially large, and decreases with the lapse of time, so that, from the viewpoints of environmental purification, sterilization or disinfection of bacteria or virus and the like, and deodorization, antifungal, and antisepsis and the like of indoor, outdoor or food and the like in house or hospital and the like, the generation holding time of the chlorine dioxide gas is required to be further increased.

It is an object of the present invention to provide a method for generating a chlorine dioxide gas, a kit for generating a chlorine dioxide gas, and a gel composition which suppress the initial rapid generation of the chlorine dioxide gas and stably hold the generation of the chlorine dioxide gas for an extremely long time.

Solution to Problem

An aspect of the present invention is a method for generating a chlorine dioxide gas, the method including continuously generating the chlorine dioxide gas from a gel composition obtained by adding a gelling, activator containing a gas generating agent, a gas generation controlling agent containing a carbonate and hydrogen peroxide, a gas generation adjusting agent, and a water-absorbent resin to a chlorite aqueous solution.

In the method according to the aspect of the present invention, the gel composition may have a flat surface from which the chlorine dioxide gas is generated. The chlorite aqueous solution may be enclosed in an airtight container before the gelling activator is added. The gelling activator may be enclosed in an airtight container before being added to the chlorite aqueous solution.

Another aspect of the present invention is a kit for generating a chlorine dioxide gas, the kit including: an agent (A) containing a chlorite aqueous solution; and an agent (B) containing a gelling, activator containing a gas generating agent, a gas generation controlling agent containing a carbonate and hydrogen peroxide, a gas generation adjusting agent, and a water-absorbent resin, wherein the chlorine dioxide gas is continuously generated by adding the agent (B) to the agent (A).

Still another aspect of the present invention is a gel composition including: a chlorite aqueous solution; and a gelling activator containing a gas generating agent, a gas generation controlling agent containing a carbonate and hydrogen peroxide, a gas generation adjusting agent, and a water-absorbent resin, wherein a chlorine dioxide gas is continuously generated.

In the gel composition according to the aspect of the present invention, the gel composition may have a flat surface from which the chlorine dioxide gas is generated.

Advantageous Effect of Invention

According to the present invention, there is provided a method for generating a chlorine dioxide gas, a kit for generating a chlorine dioxide gas, and a gel composition which suppress the initial rapid generation of the chlorine dioxide gas and stably hold the generation of the chlorine dioxide gas for an extremely long time.

›BRIEF DESCRIPTION OF DRAWINGS

FIG. 1 is a schematic diagram showing an example of a container including a gel composition.

FIG. 2 is a schematic diagram showing a method for measuring the concentration of a chlorine dioxide gas generated from a gel composition.

FIG. 3 is a graph showing a time-dependent change in the concentration of a chlorine dioxide gas generated by the lapse of 240 hours from the addition of a gelling activator to a chlorite aqueous solution in Comparative Example 1 and Example 1.

FIG. 4 is a graph showing a time-dependent change in the concentration of a chlorine dioxide gas generated by the lapse of 2,600 hours from the addition of a gelling activator to a chlorite aqueous solution in Comparative Example 1 and Example 1.

FIG. 5 is a graph showing a time-dependent change in the concentration of a chlorine dioxide gas generated by the lapse of 240 hours from the addition of a gelling activator to a chlorite aqueous solution in Comparative Example 2 and Example 2.

FIG. 6 is a graph showing a time-dependent change in the concentration of a chlorine dioxide gas generated by the lapse of 2,600 hours from the addition of a gelling activator to a chlorite aqueous solution in Comparative Example 2 and Example

FIG. 7 is a graph showing a time-dependent change in the concentration of a chlorine dioxide gas generated by the lapse of 240 hours from the addition of a gelling activator to a chlorite aqueous solution in Comparative Example 3 and Example 3.

FIG. 8 is a graph showing a time-dependent change in the concentration of a chlorine dioxide gas generated by the lapse of 2,600 hours from the addition of a gelling activator to a chlorite aqueous solution in Comparative Example 3 and Example 3.

FIG. 9 is a graph showing a time-dependent change in the concentration of a chlorine dioxide gas generated by the lapse of 720 hours from the addition of a gelling activator to a chlorite aqueous solution in Example 4.

FIG. 10 is a graph showing a time-dependent change in the concentration of a chlorine dioxide gas generated by the lapse of 720 hours from the addition of a gelling activator to a chlorite aqueous solution in Example 5.

FIG. 11 is a graph showing a time-dependent change in the concentration of a chlorine dioxide gas generated by the lapse of 720 hours from the addition of a gelling activator to a chlorite aqueous solution in Example 6.

DESCRIPTION OF EMBODIMENTS
›Embodiment 1 · 1 of 4

Method for Generating Chlorine Dioxide Gas

A method for generating a chlorine dioxide gas according to an embodiment of the present invention, the method includes continuously generating the chlorine dioxide gas from a gel composition obtained by adding a gelling activator containing a gas generating agent, a gas generation controlling agent containing a carbonate and hydrogen peroxide, a gas generation adjusting agent, and a water-absorbent resin to a chlorite aqueous solution. In the method for generating a chlorine dioxide gas of the present embodiment, the gas generation controlling agent and the gas generation adjusting agent can suppress the initial rapid generation of the chlorine dioxide gas, and stably hold the generation of the chlorine dioxide gas for an extremely long time. Herein, the term “initial” means, for example, a period by the lapse of 72 hours (particularly, the lapse of 24 hours) from the addition of the gelling activator to the chlorite aqueous solution.

In the method for generating a chlorine dioxide gas of the present embodiment, it is specified that “adding the gelling activator to the chlorite aqueous solution”, but by “adding the chlorite aqueous solution to the gelling activator”, essentially the same function effect can be obtained. That is, the case of “adding the chlorite aqueous solution to the gelling activator” is equivalent to the case of “adding the gelling activator to the chlorite aqueous solution”.

In the method for generating a chlorine dioxide gas of the present embodiment, from the viewpoint of stably holding the generation of the chlorine dioxide gas for an extremely long time, it is preferable that the gel composition has a flat surface from which the chlorine dioxide gas is generated.

In the method for generating a chlorine dioxide gas of the present embodiment, from the viewpoint that the production and generation of the chlorine dioxide gas due to the decomposition of the chlorite in the chlorite aqueous solution before the gelling activator is added can be suppressed to stably preserve the chlorite aqueous solution for a long period of time, and the gelling activator is added to stably and continuously generate the chlorine dioxide gas for a long time, it is preferable that the chlorite aqueous solution is enclosed in an airtight container before the gelling activator is added.

In the method for generating a chlorine dioxide gas of the present embodiment, from the viewpoints of making it possible to suppress the deterioration of the gelling activator before being added to the chlorite aqueous solution to stably preserve the gelling activator for a long time, and of adding the gelling activator to the chlorite aqueous solution to stably and continuously generate the chlorine dioxide gas for a long time, it is preferable that the gelling activator is enclosed in the airtight container before being added to the chlorite aqueous solution.

Chlorite Aqueous Solution

The chlorite aqueous solution used in the method for generating a chlorine dioxide gas of the present embodiment is a liquid containing a chlorite, and contains water as a main component (meaning that the content of water in a solvent and/or a dispersion medium excluding a solute and/or a dispersoid such as a chlorite is greater than or equal to 50% by mass, the same applies to the following). The chlorite aqueous solution can dissolve and/or disperse a gelling activator containing a gas generating agent, a gas generation controlling agent, a gas generation adjusting agent, and a water-absorbent resin. By adding the gelling activator to the chlorite aqueous solution, a gel composition is formed, and the chlorine dioxide gas is continuously generated from the formed gel composition via its surface. From the viewpoint of safely, stably, and continuously generating the chlorine dioxide gas for a long time from the gel composition gelled by adding the gelling activator to the chlorite aqueous solution, it is preferable that the chlorite aqueous solution is an aqueous solution or an aqueous dispersion.

The chlorite contained in the chlorite aqueous solution is not particularly limited as long as it generates the chlorine dioxide gas due to the presence of the gas generating agent described later. Examples thereof include chlorites of Group 1 elements (alkali metal elements) except hydrogen such as sodium chlorite (NaClO 2 ), potassium chlorite (KClO 2 ), and lithium chlorite (LiClO 2 ), and chlorites of Group 2 elements such as calcium chlorite (Ca(ClO 2 ) 2 ), strontium chlorate (Sr(ClO 2 ) 2 ), barium chlorite (Ba(ClO 2 ) 2 ), and magnesium chlorite (Mg(ClO 2 ) 2 ). Among these, commercially available sodium chlorite is readily available, which causes no problem in use.

The chlorite aqueous solution is obtained by dissolving the above chlorite in a predetermined concentration in an aqueous solution. When sodium chlorite is dissolved in an aqueous solution, a commercially available 25% by mass sodium chlorite aqueous solution used as a bleaching agent is suitably used as a liquid, and a commercially available 86% by mass product, a 80% by mass product, a 79% by mass product, or a 76% by mass product is suitably used as a solid. From the viewpoint that the chlorite aqueous solution does not correspond to a poisonous substance and a hazardous substance, and is easily treated, the concentration of the chlorite aqueous solution is preferably less than 25% by mass, more preferably less than 15% by mass, and still more preferably less than or equal to 10% by mass.

The chlorite aqueous solution is preferably alkaline, more preferably has a pH of greater than or equal to 9 and less than or equal to 13, and still more preferably has a pH of greater than or equal to 10 and less than or equal to 12.5. It is possible to suppress the production and generation of the chlorine dioxide gas due to the decomposition of the chlorite in the chlorite aqueous solution before the addition of the gelling activator to stably preserve the chlorite aqueous solution for a long period of time, and to add the gelling activator to stably and continuously generate the chlorine dioxide gas for a long of time.

›Embodiment 1 · 2 of 4

It is preferable that the chlorite aqueous solution further contains an alkaline agent in order to make the chlorite aqueous solution alkaline. The alkaline agent is not particularly limited as long as the alkaline agent is dissolved and/or dispersed in the chlorite aqueous solution to cause the chlorite aqueous solution to exhibit alkalinity, but from the viewpoint that, by adding the gelling activator, the generation of the chlorine dioxide gas is not hindered even under an acidic atmosphere, sodium hydroxide (NaOH) and potassium hydroxide (KOH) and the like are preferred. Potassium hydroxide is particularly preferred from the viewpoint that potassium hydroxide, unlike sodium hydroxide, does not react with carbon dioxide in the atmosphere to form a salt such as sodium bicarbonate, and from the viewpoint that potassium hydroxide is likely to wet, penetrate, and being mixed with the gelling activator during hydration as compared with sodium hydroxide, to further facilitate the formation of the gel composition.

It is preferable that the chlorite aqueous solution is enclosed in the airtight container before the gelling activator is added. By enclosing the chlorite aqueous solution in the airtight container, the generation of the chlorine dioxide gas due to the decomposition of the chlorite in the chlorite aqueous solution before the addition of the gelling activator can be suppressed, to stably preserve the chlorite aqueous solution for a long period of time, and by adding the gelling activator, the chlorine dioxide gas can be stably and continuously generated for a long time. Herein, the airtight container means a container not permeating a gas such as water vapor, a liquid such as moisture, and a solid. Specifically, the airtight container means a container having a mass change of less than or equal to 0.7 g before and after being allowed to stand in a thermostatic chamber at 50° C. for 2 months (60 days) in a state where the container encloses 85 g of a 8.7% by mass sodium chlorite aqueous solution. From the viewpoints of low reactivity with the chlorite aqueous solution and stable preservation of the chlorite aqueous solution for a long period of time, various plastic containers are preferred.

Gas Generating Agent

The gas generating agent used in the method for generating a chlorine dioxide gas of the present embodiment has a function of stably keeping a pH atmosphere in the gel composition in a weak alkali state or acidic state required for generating the chlorine dioxide gas from the chlorite, to generate chlorine dioxide. The gas generating agent is a constituent of the gelling activator, and is a solid. Herein, the pH atmosphere in the gel composition is not particularly limited, and from the viewpoint of stably and continuously producing the chlorine dioxide gas for a long time, the pH atmosphere has preferably a pH of greater than or equal to 2 and less than or equal to 9, and more preferably a pH of greater than or equal to 3 and less than or equal to 7.

The gas generating agent is not particularly limited, and from the viewpoint of preferably keeping the pH atmosphere in the gel composition at greater than or equal to 2 and less than or equal to 9 to stably and continuously produce the chlorine dioxide gas for a long time, the gas generating agent preferably contains at least one substance selected from the group consisting of a salt of a weak acid having an acid dissociation constant pK a of greater than or equal to 2.5, a weak acid having an acid dissociation constant pK a of greater than or equal to 3.8, an amphoteric compound having both acidic and alkaline functional groups, and a heterocyclic compound having a pyrimidine structure.

Examples of the salt of a weak acid having an acid dissociation constant pK a of greater than or equal to 2.5 include sodium citrate as a salt of citric acid (pK a1 : 2.90, pK a2 : 4.35, pK a3 : 5.69), and sodium malate as a salt of malic acid (pK a1 : 3.23, pK a1 : 4.77). Herein, there are three kinds of sodium citrates: monosodium citrate, disodium citrate, and trisodium citrate. Among these, disodium citrate and trisodium citrate are more preferred. There are two kinds of sodium malates: monosodium malate and disodium malate. Among these, disodium malate is more preferred. Herein, the salt of a weak acid may be an anhydrous salt or a water-containing salt.

Examples of the weak acid having an acid dissociation constant pK a of greater than or equal to 3.8 include succinic acid (pK a1 : 3.99, pK a2 : 5.20), and boric acid (pK a1 : 9.23, pK a2 : 12.74, pK a3 : 13.52).

Examples of the amphoteric compound include amino acids having a carboxyl group (COOH group) as an acidic functional group, and an amino group (NH 2 group) as an alkaline functional group. Examples of the amino acids include glycine, alanine, valine, leucine, and isoleucine having an alkyl chain, serine and triionine having a hydroxy group (OH group), asparagine and glutamine having an amide group (RCONH group), proline having an imino group (C═NH group or CNHC group), phenylalanine, tyrosine and tryptophan having a phenyl group (C 6 H 5 group), aspartic acid and glutamic acid having greater than or equal to two carboxyl groups (COOH group), and ricin and arginine having greater than or equal to two amino groups (NH 2 group).

Examples of the heterocyclic compound having a pyrimidine structure include barbituric acid, and orotic acid.

From the viewpoint of stably and continuously promoting the production of the chlorine dioxide gas for a long time while preferably keeping the pH atmosphere in the gel composition at greater than or equal to 2 and less than or equal to 9, the gas generating agent preferably further contains a weak acid having an acid dissociation constant pK a of greater than or equal to 2.5 and a first acid dissociation constant pK a1 of less than 3.8. From the viewpoint of high safety, the weak acid is preferably organic acid used as a food additive. Examples of the organic acid having an acid dissociation constant pK a of greater than or equal to 2.5 and a first acid dissociation constant pK a1 of less than 3.8 include carboxylic acids such as citric acid (pK a1 : 2.90, pK a2 : 4.35, pK a3 : 5.69), malic acid (pK a1 : 3.23, pK a2 : 4.77), formic acid (pK a1 : 3.54), lactic acid (pK a1 : 3.64), and tartaric acid (in a (+) form, pK a1 : 2.87, pK a2 : 3.97: in a meso form, pK a1 : 2.95, pK a2 : 4.46).

›Embodiment 1 · 3 of 4

Herein, when the salt of a weak acid having an acid dissociation constant pK a of greater than or equal to 2.5 and the weak acid having an acid dissociation constant pK a of greater than or equal to 2.5 and a first acid dissociation constant pK a1 of less than 3.8 are used, from the viewpoint of more stably maintaining the pH atmosphere in the gel composition, the salt of a weak acid and the weak acid are preferably conjugate salts and acids. For example, when a citrate salt is used as the salt of a weak acid, it is preferable to use citric acid as the weak acid, and when a malate is used as the salt of a weak acid, it is preferable to use malic acid as the weak acid.

Gas Generation Controlling Agent

The gas generation controlling agent used in the method for generating a chlorine dioxide gas of the present embodiment has a function of controlling the generation of the chlorine dioxide from the chlorite due to the gas generating agent according to a chemical action. The gas generation controlling agent is a constituent of the gelling activator, and is a solid. The gas generation controlling agent contains a carbonate and hydrogen peroxide. The carbonate contained in the gas generation controlling agent reacts with the gas generating agent for stably keeping the pH atmosphere in the gel composition in a weak alkali state or acidic state required for the generation of the chlorine dioxide gas from the chlorite to generate a carbon dioxide gas. This suppresses the rapid generation of the chlorine dioxide gas in the initial formation of the gel composition obtained by adding the gelling activator to the chlorite aqueous solution. Since the generated carbon dioxide gas is released from the surface of the gel composition, the gel composition has a constant flat surface. Therefore, the chlorine dioxide gas is stably and continuously generated for a long time from the gel composition via the surface. Hydrogen peroxide contained in the gas generation controlling agent decreases the generated chlorine dioxide gas by reducing. This suppresses the rapid generation of the chlorine dioxide gas in the initial formation of the gel composition obtained by adding the gelling activator to the chlorite aqueous solution.

The gas generation controlling agent containing a carbonate and hydrogen peroxide is not particularly limited, and from the viewpoint of suppressing the rapid generation of the chlorine dioxide from the chlorite to stably maintain the generation of the chlorine dioxide for a long time, sodium carbonate hydrogen peroxide (denoted as Na 2 CO 3 .1.5H 2 O 2 or 2Na 2 CO 3 .3H 2 O 2 ), and potassium carbonate hydrogen peroxide (denoted as K 2 CO 3 .1.5H 2 O 2 or 2K 2 CO 3 .3H 2 O 2 ) and the like are preferred, and from the viewpoint of easy availability, sodium carbonate hydrogen peroxide is more preferred. Herein, sodium carbonate hydrogen peroxide refers to an adduct compound in which sodium carbonate and hydrogen peroxide are mixed at a molar ratio of 2:3, and is referred to as a sodium carbonate hydrogen peroxide adduct according to the Japanese law.

Gas Generation Adjusting Agent

The gas generation adjusting agent used in the method for generating a chlorine dioxide gas of the present embodiment has a function of adjusting the generation of the chlorine dioxide from the chlorite due to the gas generating agent according to a physical action. That is, the gas generation adjusting agent has functions of maintaining at least part of the chlorine dioxide gas in the surface of the gel composition and/or in the gel composition when the amount of the chlorine dioxide gas generated from the chlorite is large, and of releasing the chlorine dioxide gas maintained when the amount of the chlorine dioxide gas generated from the chlorite is small or zero, to continuously generate the chlorine dioxide gas from the gel composition. The gas generation adjusting agent is a constituent of the gelling activator, and is a solid.

The material and shape of the gas generation adjusting agent are not particularly limited as long as the gas generation adjusting agent can efficiently disperse the generation of the chlorine dioxide gas, and from the viewpoint of being capable of maintaining a large amount of the chlorine dioxide gas, the gas generation adjusting agent is preferably a porous material having a large surface area. At least one selected from the group consisting of sepiolite, montmorillonite, diatomaceous earth, talc, and zeolite is preferred. From the viewpoint of increasing the surface area, the gas generation adjusting agent is preferably powdery, granular and/or porous.

Among the gas generation adjusting agents, from the viewpoint of excellent holding and release of the chlorine dioxide gas, sepiolite is preferred. Herein, sepiolite is a natural mineral of a magnesium silicate salt, and its chemical composition formula is represented by Mg 8 S 12 O 30 (OH) 4 (OH 2 ) 4 .8H 2 O. Sepiolite has a fibrous crystal structure, has a large number of grooves on its surface, has a large number of clearances having a cylindrical tunnel structure, and has a very large surface area. Examples of commercially available products include Miraclay (manufactured by Omi Mining Co., Ltd.). Examples of the powdery diatomaceous earth include Celite (trade name, manufactured by Showa Chemical Co., Ltd.).

Water-Absorbent Resin

The water-absorbent resin used in the method for generating a chlorine dioxide gas of the present embodiment has a function of absorbing moisture to form the gel composition. The water-absorbent resin is a constituent of the gelling activator, and is a solid. For example, a starch-based water-absorbent resin, a cellulose-based water-absorbent resin, and a synthetic polymer-based water-absorbent resin and the like are preferably used. Examples of the starch-based water-absorbent resin include a starch/polyacrylic acid-based resin (powder manufactured by Sanyo Chemical Industries, Ltd.), and examples of the synthetic polymer-based water-absorbent resin include a crosslinked polyacrylic acid-based resin, an isobutylene/maleic acid-based resin, a poval/polyacrylate-based resin, and a polyacrylic acid-based resin. Specifically, sodium polyacrylate and the like are used.

›Embodiment 1 · 4 of 4

Gelling Activator

The gelling activator used in the method for generating a chlorine dioxide gas of the present embodiment is added to the chlorite aqueous solution to form the gel composition, and the gelling activator has a function of stably and continuously generating the chlorine dioxide gas from the formed gel composition. The gelling activator contains a gas generating agent, a gas generation controlling agent containing a carbonate and hydrogen peroxide, a gas generation adjusting agent, and a water-absorbent resin. Herein, from the viewpoint of forming a homogeneous gel composition, it is preferable that the gelling activator is added to the chlorite aqueous solution to form the gel composition, and the gelling activator has a function of stably and continuously generating the chlorine dioxide gas from the formed gel composition, and contains one obtained by sufficiently mixing a gas generating agent, a gas generation controlling agent containing a carbonate and hydrogen peroxide, a gas generation adjusting agent, and a water-absorbent resin.

The gelling activator is preferably enclosed in an airtight container before being added to the chlorite aqueous solution. Before the addition of the gelling activator to the chlorite aqueous solution, the gelling activator is enclosed in the airtight container, whereby the mixing of moisture from the atmosphere into the gelling activator is prevented, which provides prevented deterioration. Therefore, the gelling activator can be stably preserved for a long period of time. Herein, the airtight container means a container not permeating a gas such as water vapor, a liquid such as moisture, and a solid. Specifically, the airtight container means a container having a mass change of less than or equal to 0.7 g before and after being allowed to stand in a thermostatic chamber at 50° C. for 2 months (60 days) in a state where the container encloses 85 g of a 8.7% by mass sodium chlorite aqueous solution. Examples thereof include various plastic containers.

Flatness of Surface of Gel Composition from Which Chlorine Dioxide Gas is Generated

In the method for generating a chlorine dioxide gas of the present embodiment, from the viewpoint of keeping the surface area of the surface from which the chlorine dioxide gas is generated constant, to stably hold the generation of the chlorine dioxide gas for an extremely long time, the gel composition preferably has a flat surface from which the chlorine dioxide gas is generated. Herein, the flatness of the surface of the gel composition from which the chlorine dioxide gas is generated means that the surface is visually flat with no local protrusion of the surface due to the addition of the gelling activator to the chlorite aqueous solution. Furthermore, from the viewpoint of keeping the surface area of the surface from which the chlorine dioxide gas is generated constant, to stably hold the generation of the chlorine dioxide gas for an extremely long time, it is more preferable that the surface of the gel composition from which the chlorine dioxide gas is generated is flat, and cracks do not occur.

›Embodiment 2

Kit for Generating Chlorine Dioxide Gas

A kit for generating a chlorine dioxide gas according to another embodiment of the present invention is a kit including: an agent (A) containing a chlorite aqueous solution; and an agent (B) containing a gelling activator containing a gas generating agent, a gas generation controlling agent containing a carbonate and hydrogen peroxide, a gas generation adjusting agent, and a water-absorbent resin, wherein the chlorine dioxide gas is continuously generated by adding the agent (B) to the agent (A). In the kit for generating a chlorine dioxide gas of the present embodiment, the gas generation controlling agent and the gas generation adjusting agent contained in the agent (B) can suppress the initial rapid generation of the chlorine dioxide gas and stably hold the generation of the chlorine dioxide gas for an extremely long time.

In the kit for generating a chlorine dioxide gas of the present embodiment, it is specified that “adding the agent (B) to the agent (A)”, but by “adding the agent (A) to the agent (B)”, essentially the same function effect can be obtained. That is, the case of “adding the agent (A) to the agent (B)” is equivalent to the case of “adding the agent (B) to the agent (A)”.

In the kit for generating a chlorine dioxide gas of the present embodiment, from the viewpoints that the generation of the chlorine dioxide gas due to the decomposition of the chlorite in the chlorite aqueous solution in the agent (A) before the addition of the agent (B) can be suppressed to stably preserve the chlorite aqueous solution for a long period of time, and the agent (B) is added to suppress the initial rapid generation of the chlorine dioxide gas and to stably and continuously generate the chlorine dioxide gas for a long time, the chlorite aqueous solution contained in the agent (A) is preferably alkaline, more preferably has a pH of greater than or equal to 9 and less than or equal to 13, and still more preferably has a pH of greater than or equal to 10 and less than or equal to 12.5.

It is preferable that the agent (A) as one element of the kit for generating a chlorine dioxide gas of the present embodiment is enclosed in an airtight container before the addition of the agent (B). The production and generation of the chlorine dioxide gas due to the decomposition of the chlorite in the chlorite aqueous solution in the agent (A) before the addition of the agent (B) can be suppressed to stably preserve the agent (A) containing the chlorite aqueous solution for a long period of time, and the agent (B) can be added to stably and continuously generate the chlorine dioxide gas for a long time. Herein, the airtight container means a container not permeating a gas such as water vapor, a liquid such as moisture, and a solid. From the viewpoints of low reactivity with the chlorite aqueous solution and stable preservation of the chlorite aqueous solution for a long period of time, various plastic containers are preferred.

It is preferable that the agent (B) as another element constituting the kit for generating a chlorine dioxide gas of the present embodiment is enclosed in the airtight container before being added to the agent (A). The gelling activator in the agent (B) is enclosed in the airtight container, whereby the mixing of moisture from the atmosphere into the gelling activator is prevented, which provides prevented deterioration. Therefore, the agent (B) containing the gelling activator can be stably preserved for a long period of time. Herein, the airtight container means a container not permeating a gas such as water vapor, a liquid such as moisture, and a solid. Examples thereof include various plastic containers.

From the viewpoint of forming a homogeneous gel composition to continuously generate the chlorine dioxide gas for an extremely long time, it is preferable that the agent (B) contains a gelling activator obtained by sufficiently mixing a gas generating agent, a gas generation controlling agent containing a carbonate and hydrogen peroxide, a gas generation adjusting agent, and a water-absorbent resin.

In the kit for generating a chlorine dioxide gas of the present embodiment, the chlorite aqueous solution, the gas generating agent, the gas generation controlling agent containing a carbonate and hydrogen peroxide, the gas generation adjusting agent, the water-absorbent resin, and the gelling activator are the same as the chlorite aqueous solution, the gas generating agent, the gas generation controlling agent containing a carbonate and hydrogen peroxide, the gas generation adjusting agent, the water-absorbent resin, and the gelling activator in the method for generating a chlorine dioxide gas of the embodiment 1, and the descriptions thereof will not be repeated herein.

From the viewpoints of suppressing the initial rapid generation of the chlorine dioxide gas and of stably holding the generation of the chlorine dioxide gas for an extremely long time, in the kit for generating a chlorine dioxide gas of the present embodiment, it is preferable that the amounts of the agents (A) and (B) are respectively 60% by mass to 90% by mass, and 10% by mass to 40% by mass based on the whole kit. It is preferable that the amounts of a chlorite component and an aqueous solution component in the chlorite aqueous solution are respectively 2% by mass to 20% by mass and 80% by mass to 98% by mass in terms of pure content based on the whole agent (A). It is preferable that the amounts of the gas generating agent, the gas generation controlling agent, the gas generation adjusting agent, and the water-absorbent resin in the gelling activator are respectively 10% by mass to 60% by mass, 0.1% by mass to 15% by mass, 5% by mass to 60% by mass, and 15% by mass to 90% by mass based on the whole agent (B).

The specific form of the kit for generating a chlorine dioxide gas of the present embodiment is not particularly limited, and examples thereof include a form in which an airtight container enclosing the agent (A) (for example, the chlorite aqueous solution) and an airtight container enclosing the agent (B) (for example, the gelling activator containing the gas generating agent, the gas generation controlling agent containing a carbonate and hydrogen peroxide, the gas generation adjusting agent, and the water-absorbent resin) are packaged together, and a form in which one obtained by packaging a container enclosing the agent (A) (for example, the chlorite aqueous solution) and one obtained by packaging a container enclosing the agent (B) (for example, the gelling activator containing the gas generating agent, the gas generation controlling agent containing a carbonate and hydrogen peroxide, the gas generation adjusting agent, and the water-absorbent resin) are combined.

›Embodiment 3

Gel Composition

A gel composition according to still another embodiment of the present invention includes: a chlorite aqueous solution; and a gelling activator containing a gas generating agent, a gas generation controlling agent containing a carbonate and hydrogen peroxide, a gas generation adjusting agent, and a water-absorbent resin, wherein a chlorine dioxide gas is continuously generated. The gas generation controlling agent and gas generation adjusting agent contained in the gel composition of the present embodiment can suppress the initial rapid generation of the chlorine dioxide gas and stably hold the generation of the chlorine dioxide gas for an extremely long tune.

According to the method for generating a chlorine dioxide gas of the embodiment 1, the gel composition of the present embodiment is gelled by adding a gelling activator containing a gas generating agent, a gas generation controlling agent containing a carbonate and hydrogen peroxide, a gas generation adjusting agent, and a water-absorbent resin to a chlorite aqueous solution. More specifically, the gel composition of the present embodiment is gelled by adding an agent (B) containing a gelling activator containing a gas generating agent, a gas generation controlling agent containing a carbonate and hydrogen peroxide, a gas generation adjusting agent, and a water-absorbent resin to an agent (A) containing a chlorite aqueous solution, using the kit for generating a chlorine dioxide gas of the embodiment 2.

From the viewpoint of keeping the surface area of the surface from which the chlorine dioxide gas is generated constant in the gel composition of the present embodiment, to stably hold the generation of the chlorine dioxide gas for an extremely long time, the gel composition preferably has a flat surface from which the chlorine dioxide gas is generated. Herein, the flatness of the surface of the gel composition from which the chlorine dioxide gas is generated means that the surface is visually flat with no local protrusion of the surface due to the addition of the gelling activator to the chlorite aqueous solution. Furthermore, from the viewpoint of keeping the surface area of the surface from which the chlorine dioxide gas is generated constant, to stably hold the generation of the chlorine dioxide gas for an extremely long time, it is more preferable that the surface of the gel composition from which the chlorine dioxide gas is generated is flat, and cracks do not occur.

In the gel composition of the present embodiment, the chlorite aqueous solution, the gas generating agent, the gas generation controlling agent containing a carbonate and hydrogen peroxide, the gas generation adjusting agent, the water-absorbent resin, and the gelling activator are the same as the chlorite aqueous solution, the gas generating agent, the gas generation controlling agent containing a carbonate and hydrogen peroxide, the gas generation adjusting agent, the water-absorbent resin, and the gelling activator in the method for generating a chlorine dioxide gas of the embodiment 1, and the descriptions thereof will not be repeated herein.

From the viewpoints of suppressing the initial rapid generation of the chlorine dioxide gas and of stably holding the generation of the chlorine dioxide gas for an extremely long time, in the gel composition of the present embodiment, it is preferable that the amounts of the chlorine component in the chlorite aqueous solution, the aqueous solution component in the chlorite aqueous solution, the gas generating agent, the gas generation controlling agent, the gas generation adjusting agent, and the water-absorbent resin are respectively 2.5% by mass to 10% by mass, 50% by mass to 95% by mass, 2% by mass to 15% by mass, 0.03% by mass to 3% by mass, 1.5% by mass to 15% by mass, and 2.5% by mass to 20% by mass in terms of pure content.

›EXAMPLES

Preparation of Container for Generating Chlorine Dioxide Gas

As shown in FIG. 1 , a container 1 for generating a chlorine dioxide gas was prepared, which included a plastic body 10 and a plastic lid 20 . The plastic body 10 was a substantially cylindrical container having an opening, and had a bottom portion having an outer diameter E 1 of 64 mm and an inner diameter I 1 of 60 mm, a top portion having an opening having an inner diameter I 2 of 37 mm, a cylindrical tubular body portion having a height H 1 of 64 mm and a volume of 174 ml, a truncated conical cylindrical shoulder portion having a height H 2 of 11 mm, and a cylindrical tubular neck portion having a height H 3 of 15 mm. The plastic lid 20 included an inner lid 22 having an opening 22 w and an outer lid 24 having an opening 24 w . The inner lid 22 and the outer lid 24 were disposed so as to be slidably rotatable around a central portion. An overlapping portion of the opening 22 w of the inner lid 22 and the opening 24 w of the outer lid 24 constituted an opening 1 w of the container 1 for generating a chlorine dioxide gas.

Preparation of Chlorite Aqueous Solution

As a chlorite aqueous solution, a 25% by mass sodium chlorite aqueous solution (25% sodium chlorite aqueous solution manufactured by Daiso Co., Ltd.) was diluted with pure water to prepare a 8.7% by mass sodium chlorite aqueous solution,

Preparation of Gelling Activator

As a gelling activator for examples, 3,195 g of trisodium citrate dihydrate and 1,755 g of anhydrous citric acid as a gas generating agent, 5,040 g of a polvacrylic acid-based water-absorbent resin (Sun Fresh ST-500D manufactured by Sanyo Kasei Co., Ltd.) as a water-absorbent resin, 1,800 g of a sepiolite powder (Miraclay P-150D manufactured by Omi Kogyo Co., Ltd.) as a gas generation adjusting agent, and 180 g of sodium carbonate hydrogen peroxide as a gas generation controlling agent were uniformly mixed to prepare a mixed powder. As a gelling activator for comparative examples, one obtained by removing sodium carbonate hydrogen peroxide as the gas generation controlling agent from the gelling activator for examples was uniformly mixed to prepare a mixed powder.

›Examples6
›Example 1

In a thermostatic chamber having a temperature of 20.3° C. and a humidity (referred to as relative humidity, the same applies to the following) of 69%, 117.25 g of the chlorite aqueous solution (8.8% by mass of sodium chlorite aqueous solution) was placed in a plastic body 10 of a container 1 for generating a chlorine dioxide gas shown in FIG. 1 , and 33.25 g of the gelling activator for examples (for the composition of each component, trisodium citrate dihydrate: 8.875 g, anhydrous citric acid: 4.875 g, polyacrylic acid-based water-absorbent resin: 14 g, sepiolite powder: 5 g, sodium carbonate hydrogen peroxide: 0.5 g) was then added. Thereafter, an opening 10 w of the plastic body 10 was covered with a plastic lid 20 , and an inner lid 22 and an outer lid 24 were disposed such that an opening 1 w of an overlapping portion of an opening 22 w of the inner lid 22 and an opening 24 w of the outer lid 24 become maximum. The maximum opening 1 w of the container 1 for generating a chlorine dioxide gas had a substantially trapezoidal shape, had an upper base of 7 mm, a lower base of 10 mm, and a height of 5 mm, and had an area of 42.5 mm 2 . After 4 minutes from the addition of the gelling activator to the chlorite aqueous solution, the chlorite aqueous solution was gelled to obtain a gel composition 30 . A gel time was 4 minutes. A surface 30 s of the obtained gel composition 30 was flat (visually flat with no local protrusion of the surface due to the addition of the gelling activator for examples to the chlorite aqueous solution). No cracks occurred in the surface 30 s of the gel composition 30 .

Next, the container 1 for generating a chlorine dioxide gas containing the chlorite aqueous solution and the gelling activator for examples was placed in a beaker 2 having a volume of 1 liter, and the beaker 2 was covered with a plastic film 3 excluding a pouring spout portion of the beaker. Then, the beaker including the container 1 for generating a chlorine dioxide gas in which the gel composition was formed was allowed to stand in a thermostatic chamber having a temperature of 19.7° C. to 20.7° C. and a relative humidity of 36% to 88%, and a Kitagawa type detecting tube 4 was inserted from the pouring spout of the beaker after the lapse of a predetermined time from the addition of the gelling activator for examples to the chlorite aqueous solution to measure the concentration of the generated chlorine dioxide gas, thereby examining its time-dependent change. The results were shown in Tables 1 and 2 and FIGS. 3 and 4 .

Comparative Example 1

A gel composition was formed in the same manner as in Example 1 except that, in place of 33.25 g of the gelling activator for examples, 32.75 g of the gelling activator for comparative examples (for the composition of each component, trisodium citrate dihydrate: 8.875 g, anhydrous citric acid: 4.875 g, polyacrylic acid-based water-absorbent resin: 14 g, sepiolite powder: 5 g) was used. A gel time was 4 minutes. In the surface of the obtained gel composition, local protrusion was formed by the addition of the gelling activator for comparative examples to a chlorite aqueous solution. Cracks occurred in the surface of the gel composition.

Then, in the same manner as in Example 1, the concentration of the generated chlorine dioxide gas was measured after the lapse of a predetermined time from the addition of the gelling activator for comparative examples to the chlorite aqueous solution, to examine its time-dependent change. The results were summarized in Tables 1 and 2 and FIGS. 3 and 4 .

With reference to Table 1 and FIG. 3 , in Comparative Example 1, the concentration of the chlorine dioxide initially generated by the lapse of 72 hours from the addition of the gelling activator for Comparative Example 1 to the chlorite aqueous solution (particularly by the lapse of 24 hours) was high, but in Example 1, the concentration of the chlorine dioxide initially generated by the lapse of 72 hours from the addition of the gelling activator for Example 1 to the chlorite aqueous solution (particularly by the lapse of 24 hours) was low. That is, in Example 1, by adding the gas generation controlling agent containing a carbonate and hydrogen peroxide in addition to the gas generation adjusting agent, the initial rapid generation of the chlorine dioxide gas after the addition of the gelling activator to the chlorite aqueous solution could be suppressed as compared with Comparative Example 1.

With reference to Tables 1 and 2 and FIG. 4 , by the lapse of 2,600 hours from the addition of the gelling activator to the chlorite aqueous solution, the fluctuation of the concentration of the chlorine dioxide gas in Example 1 was smaller than that in Comparative Example 1. The maintenance period of the concentration of the chlorine dioxide gas of greater than or equal to about 40 ppm could be extended up to about 2,490 hours in Example 1, whereas the maintenance period of Comparative Example 1 was up to about 1,918 hours. That is, in Example 1, the chlorine dioxide gas could be continuously and stably generated for an extremely long time by adding the gas generation controlling agent containing a carbonate and hydrogen peroxide in addition to the gas generation adjusting agent. Therefore, according to Example 1, a method for generating a chlorine dioxide gas, a kit for generating a chlorine dioxide gas, and a gel composition were obtained, which could continuously and stably generate the chlorine dioxide gas for a long period of time of at least 2,160 hours (90 days).

›Example 2

A gel composition was formed in the same manner as in Example 1 except that, to the 70.32 g of the chlorite aqueous solution (8.8% by mass sodium chlorite aqueous solution), 19.95 g of the gelling activator for examples (for the composition of each component, trisodium citrate dihydrate: 5.325 g, anhydrous citric acid: 2.925 g, polyacrylic acid-based water-absorbent resin: 8.4 g, sepiolite powder: 3 g, sodium carbonate hydrogen peroxide: 0.3 g) was added. A gel time was 3 minutes. A surface of the obtained gel composition was flat (visually flat with no local protrusion of the surface due to the addition of the gelling activator for examples to the chlorite aqueous solution). No cracks occurred in the surface of the gel composition.

Then, in the same manner as in Example 1, the concentration of the generated chlorine dioxide gas was measured after the lapse of a predetermined time from the addition of the gelling activator for examples to the chlorite aqueous solution, to examine its time-dependent change. The results were summarized in Tables 3 and 4 and FIGS. 5 and 6 .

Comparative Example 2

A gel composition was formed in the same manner as in Example 2 except that, in place of 19.95 g of the gelling activator for examples, 19.65 g of the gelling activator for comparative examples (for the composition of each component, trisodium citrate dihydrate: 5.325 g, anhydrous citric acid: 2.925 g, polyacrylic acid-based water-absorbent resin: 8.4 g, sepiolite powder: 3 g) was used. A gel time was 3 minutes. In the surface of the obtained gel composition, local protrusion was formed by the addition of the gelling activator for comparative examples to a chlorite aqueous solution. Cracks occurred in the surface of the gel composition.

Then, in the same manner as in Example 1, the concentration of the generated chlorine dioxide gas was measured after the lapse of a predetermined time from the addition of the gelling activator for comparative examples to the chlorite aqueous solution, to examine its time-dependent change. The results were summarized in Tables 3 and 4 and FIGS. 5 and 6 .

With reference to Table 3 and FIG. 5 , in Comparative Example 2, the concentration of the chlorine dioxide initially generated by the lapse of 56 hours from the addition of the gelling activator for comparative examples to the chlorite aqueous solution (particularly by the lapse of 24 hours) was high, but in Example 2, the concentration of the chlorine dioxide initially generated by the lapse of 56 hours from the addition of the gelling activator for comparative examples to the chlorite aqueous solution (particularly by the lapse of 24 hours) was low. That is, in Example 2, by adding the gas generation controlling agent containing a carbonate and hydrogen peroxide in addition to the gas generation adjusting agent, the initial rapid generation of the chlorine dioxide gas after the addition of the gelling activator to the chlorite aqueous solution could be suppressed as compared with Comparative Example 2.

With reference to Tables 3 and 4 and FIG. 6 , by the lapse of 2,600 hours from the addition of the gelling activator to the chlorite aqueous solution, the fluctuation of the concentration of the chlorine dioxide gas in Example 2 was smaller than that in Comparative Example 2. The maintenance period of the concentration of the chlorine dioxide gas of greater than or equal to about 40 ppm could be extended up to about 1,616 hours in Example 2, whereas the maintenance period of Comparative Example 2 was up to about 1,257 hours. That is, in Example 2, the chlorine dioxide gas could be continuously and stably generated for an extremely long time by adding the gas generation controlling agent containing a carbonate and hydrogen peroxide in addition to the gas generation adjusting agent. Therefore, according to Example 2, a method for generating a chlorine dioxide gas, a kit for generating a chlorine dioxide gas, and a gel composition were obtained, which could continuously and stably generate the chlorine dioxide gas for a long period of time of at least 1,440 hours (60 days).

›Example 3

A gel composition was formed in the same manner as in Example 1 except that, to 46.88 g of the chlorite aqueous solution (8.8% by mass sodium chlorite aqueous solution), 13.30 g of the gelling activator for examples (for the composition of each component, trisodium citrate dihydrate: 3.55 g, anhydrous citric acid: 1.95 g, polyacrylic acid-based water-absorbent resin: 5.6 g, sepiolite powder: 2 g, sodium carbonate hydrogen peroxide: 0.2 g) was added. A gel time was 2 minutes. A surface of the obtained gel composition was flat (visually flat with no local protrusion of the surface due to the addition of the gelling activator for examples to the chlorite aqueous solution). No cracks occurred in the surface of the gel composition.

Then, in the same manner as in Example 1, the concentration of the generated chlorine dioxide gas was measured after the lapse of a predetermined time from the addition of the gelling activator for examples to the chlorite aqueous solution, to examine its time-dependent change. The results were summarized in Tables 5 and 6 and FIGS. 7 and 8 .

Comparative Example 3

A gel composition was formed in the same manner as in Example 2 except that, in place of 13.30 g of the gelling activator for examples, 13.10 g of the gelling activator for comparative examples (for the composition of each component, trisodium citrate dihydrate: 3.55 g, anhydrous citric acid: 1.95 g, polyacrylic acid-based water-absorbent resin: 5.6 g, sepiolite powder: 2 g) was used. A gel time was 2 minutes. In the surface of the obtained gel composition, local protrusion was formed by the addition of the gelling activator for comparative examples to a chlorite aqueous solution. Cracks occurred in the surface of the gel composition.

Then, in the same manner as in Example 1, the concentration of the generated chlorine dioxide gas was measured after the lapse of a predetermined time from the addition of the gelling activator for comparative examples to the chlorite aqueous solution, to examine its time-dependent change. The results were summarized in Tables 5 and 6 and FIGS. 7 and 8 .

With reference to Table 5 and FIG. 7 , in Comparative Example 3, the concentration of the chlorine dioxide initially generated by the lapse of 56 hours from the addition of the gelling activator for comparative examples to the chlorite aqueous solution (particularly by the lapse of 24 hours) was high, but in Example 3, the concentration of the chlorine dioxide initially generated by the lapse of 56 hours from the addition of the gelling activator for comparative examples to the chlorite aqueous solution (particularly by the lapse of 24 hours) was low. That is, in Example 3, by adding the gas generation controlling agent containing a carbonate and hydrogen peroxide in addition to the gas generation adjusting agent, the initial rapid generation of the chlorine dioxide gas after the addition of the gelling activator to the chlorite aqueous solution could be suppressed as compared with Comparative Example 3.

With reference to Tables 5 and 6 and FIG. 8 , by the lapse of 2,600 hours from the addition of the gelling activator to the chlorite aqueous solution, the fluctuation of the concentration of the chlorine dioxide gas in Example 3 was smaller than that in Comparative Example 3. The maintenance period of the concentration of the chlorine dioxide gas of greater than or equal to about 40 ppm could be extended up to about 1,149 hours in Example 3, whereas the maintenance period of Comparative Example 3 was up to about 836 hours. That is, in Example 3, the chlorine dioxide gas could be continuously and stably generated for an extremely long time by adding the gas generation controlling agent containing a carbonate and hydrogen peroxide in addition to the gas generation adjusting agent. Therefore, according to Example 3, a method for generating a chlorine dioxide gas, a kit for generating a chlorine dioxide gas, and a gel composition were obtained, which could continuously and stably generate the chlorine dioxide gas for a long period of time of at least 1,080 hours (45 days).

›Example 4

A gel composition was formed in the same manner as in Example 1 except that 117.25 g of a 9.0% by mass sodium chlorite aqueous solution was used as a chlorite aqueous solution, and 33.55 g of a mixed powder containing 8.125 g of trisodium citrate dehydrate, 4.875 g of anhydrous citric acid, 14.5 g of a polyacrylic acid water-absorbent resin, 5.25 g of a sepiolite powder, and 0.8 g of sodium carbonate hydrogen peroxide was used as a gelling activator for examples. A gel time was 4 minutes. A surface of the obtained gel composition was flat (visually flat with no local protrusion of the surface due to the addition of the gelling activator for examples to the chlorite aqueous solution). No cracks occurred in the surface of the gel composition.

Then, in the same manner as in Example 1, the concentration of the generated chlorine dioxide gas was measured after the lapse of a predetermined time from the addition of the gelling activator for examples to the chlorite aqueous solution, to examine its time-dependent change. The results were summarized in Table 7 and FIG. 9 .

›Example 5

A gel composition was formed in the same manner as in Example 4 except that 33.35 g of a mixed powder containing 8.125 g of trisodium citrate dehydrate, 4.875 g of anhydrous citric acid, 14.5 g of a polyacrylic acid-based water-absorbent resin, 5.25 g of a sepiolite powder, and 0.6 g of sodium carbonate hydrogen peroxide was used as a gelling activator for examples. A gel time was 4 minutes. A surface of the obtained gel composition was flat (visually flat with no local protrusion of the surface due to the addition of the gelling activator for examples to the chlorite aqueous solution). No cracks occurred in the surface of the gel composition.

Then, in the same manner as in Example 1, the concentration of the generated chlorine dioxide gas was measured after the lapse of a predetermined time from the addition of the getting activator for examples to the chlorite aqueous solution, to examine its time-dependent change. The results were summarized in Table 8 and FIG. 10 .

›Example 6

A gel composition was formed in the same manner as in Example 4 except that 33.05 g of a mixed powder containing 8.125 g of trisodium citrate dehydrate, 4.875 g of anhydrous citric acid, 14.5 g of a polyacrylic acid-based water-absorbent resin, 5.25 g of a sepiolite powder, and 0.3 g of sodium carbonate hydrogen peroxide was used as a gelling activator for examples. A gel time was 4 minutes. A surface of the obtained gel composition was flat (visually flat with no local protrusion of the surface due to the addition of the gelling activator for examples to the chlorite aqueous solution). No cracks occurred in the surface of the gel composition.

Then, in the same manner as in Example 1, the concentration of the generated chlorine dioxide gas was measured after the lapse of a predetermined time from the addition of the getting activator for examples to the chlorite aqueous solution, to examine its time-dependent change. The results were summarized in Table 9 and FIG. 11 .

With reference to Tables 7 to 9 and FIGS. 9 to 11 , in any of Examples 4 to 6, a method for generating a chlorine dioxide gas, a kit for generating a chlorine dioxide gas, and a gel composition were obtained, which suppressed the initial rapid generation of the chlorine dioxide gas by the lapse of 72 hours after the addition of the gelling activator for examples to the chlorite aqueous solution (particularly, the lapse of 24 hours) and could continuously and stably generate the chlorine dioxide gas for a long period of time of at least 720 hours (30 days).

It should be understood that the embodiment and examples disclosed herein are illustrative and non-restrictive in all respects. The scope of the present invention is defined by the claims, rather than the embodiments and examples above, and is intended to include any modifications within the meaning and scope equivalent to the claims.

›REFERENCE SIGNS LIST

1 : container for generating a chlorine dioxide gas, 1 w , 10 w , 22 w , 24 w : opening, 2 : beaker, 3 : plastic film, 4 : Kitagawa type detecting tube, 10 : plastic body, 20 : plastic lid, 22 : inner lid, 24 : outer lid, 30 : gel composition, 30 s : surface

›Tables in the description — 9
TABLE 1 — ClO 2 concentration (ppm)
Lapse timeTemperatureHumidityComparative
(hr)(° C.)(%)Example 1Example 1
020.36900
0.520.3694239
120.3695042
2.520.6746545
520.1707038
820.2695835
1120.6696535
2220.4776036
5620.7766556
7120.0706058
9520.0755956
11920.2776355
14320.4786353
19120.4715653
21520.4705856
23920.2705956
28720.0796457
32420.1716057
34820.2786057
37219.8706057
39619.8866158
41419.9745558
43819.9806158
46220.0775556
49120.2805456
50920.0825455
52420.0835555
56420.1845155
60020.1845556
62420.1874554
64819.8864654
67220.2885155
69620.2844555
72020.0844555
74419.9825555
76820.1845456
80420.3845455
81219.9845455
83620.2845055
87519.9854954
88320.1844855
90720.0845055
93120.2815054
95520.1844554
98120.2874655
100520.0844352
102920.1844052
106619.9844552
107720.1845053
110119.9855053
112520.0744852
114919.9744452
117319.9704451
119619.9644552
123319.9614550
125720.2634049
126819.9634450
129220.1724551
131719.9794550
134220.0794348
136619.9803846
138520.0763846
141419.8724044
143819.8674144
146219.9624043
148620.0694043
TABLE 2 — ClO 2 concentration (ppm)
Lapse timeTemperatureHumidityComparative
(hr)(° C.)(%)Example 1Example 1
150720.0694043
154719.8584043
156319.9634044
157919.9694444
161619.7553944
163519.9563843
165319.9613842
167719.9603842
170119.9583842
172519.9573842
175920.0544042
178320.0574042
180719.8524041
181919.8503841
184319.8523841
186719.7504042
189120.0564042
191820.0554042
194019.8573842
196219.9633641
198619.9513340
201019.9423239
202420.0493340
205720.0403539
208320.1573640
210719.9653340
211520.1703240
213119.9653340
214420.1653540
215519.9653540
217920.0633240
219120.0653240
220320.2493140
221620.0503241
222619.9462940
223919.9483040
225019.9433040
226420.1503540
227520.0523440
228820.1553440
229820.0503040
231220.0453040
232220.1433039
233620.0433040
234620.0403040
236020.0453040
237020.0452940
238420.1513540
239420.0453040
240820.0453439
241819.9443339
243119.9463339
244220.0383038
245520.0503240
246620.0503240
247920.0503240
249019.9483340
250320.0423139
251420.0413238
252720.0402939
253820.0383036
255120.0413036
256220.0362736
257520.0402935
258620.0362836
259919.9372836
TABLE 3 — ClO 2 concentration (ppm)
Lapse timeTemperatureHumidityComparative
(hr)(° C.)(%)Example 2Example 2
020.36900
0.520.3694442
120.3695238
2.520.6746446
520.1706041
820.2695839
1120.6695839
2220.4775641
5620.7765455
7120.0705856
9520.0755354
11920.2775052
14320.4785653
19120.4715054
21520.4705555
23920.2705555
28720.0795655
32420.1715856
34820.2785655
37219.8705454
39619.8865555
41419.9745556
43819.9805556
46220.0774954
49120.2805052
50920.0825253
52420.0835153
56420.1845052
60020.1845052
62420.1874650
64819.8864350
67220.2884851
69620.2844250
72020.0844150
74419.9824550
76820.1845051
80420.3845051
81219.9845050
83620.2845050
87519.9854850
88320.1844550
90720.0844550
93120.2814549
95520.1844050
98120.2874549
100520.0844246
102920.1844246
106619.9844146
107720.1844246
110119.9854145
112520.0744446
114919.9744046
117319.9704046
119619.9644045
123319.9613644
125720.2634144
126819.9633643
129220.1723943
131719.9793843
134220.0793844
136619.9803439
138520.0763439
141419.8723442
143819.8673442
146219.9623442
148620.0693441
TABLE 4 — ClO 2 concentration (ppm)
Lapse timeTemperatureHumidityComparative
(hr)[° C.](%)Example 2Example 2
150720.0693441
154719.8583440
156319.9633640
157919.9693640
161619.7553540
163519.9563537
165319.9613537
167719.9603537
170119.9583537
172519.9573437
175920.0543437
178320.0573436
180719.8523335
181919.8502835
184319.8523035
186719.7503037
189120.0563437
191820.0553437
194019.8573436
196219.9633436
198619.9513236
201019.9423034
202420.0493034
205720.0403034
208320.1573235
210719.9653035
211520.1703035
213119.9653035
214420.1653135
215519.9653035
217920.0633135
219120.0653035
220320.2493035
221620.0503135
222619.9462934
223919.9483034
225019.9433034
226420.1503235
227520.0523235
228820.1553135
229820.0503035
231220.0453035
232220.1433035
233620.0432935
234620.0403135
236020.0453135
237020.0453235
238420.1513235
239420.0453235
240820.0453135
241819.9443235
243119.9463135
244220.0383034
245520.0503035
246620.0503135
247920.0503135
249019.9483034
250320.0423034
251420.0413034
252720.0402933
253820.0383033
255120.0413033
256220.0362832
257520.0402932
258620.0362932
259919.9372932
TABLE 5 — ClO 2 concentration (ppm)
Lapse timeTemperatureHumidityComparative
(hr)(° C.)(%)Example 3Example 3
020.36900
0.520.3694544
120.3694343
2.520.6746041
520.1705935
820.2695836
1120.6695636
2220.4775437
5620.7765050
7120.0705049
9520.0755050
11920.2775050
14320.4785050
19120.4715050
21520.4705051
23920.2705550
28720.0795251
32420.1715350
34820.2785450
37219.8704545
39619.8865045
41419.9744545
43819.9804545
46220.0774145
49120.2804543
50920.0824043
52420.0834344
56420.1844545
60020.1844444
62420.1873844
64819.8863344
67220.2884044
69620.2843644
72020.0843845
74419.9824045
76820.1844044
80420.3844044
81219.9844145
83620.2844045
87519.9853444
88320.1843542
90720.0843340
93120.2813441
95520.1843541
98120.2873241
100520.0842841
102920.1843442
106619.9843440
107720.1843540
110119.9853240
112520.0743541
114919.9743240
117319.9703036
119619.9643237
123319.9613238
125720.2633337
126819.9633036
129220.1723536
131719.9792336
134220.0792335
136619.9802334
138520.0762334
141419.8722634
143819.8672735
146219.9622635
148620.0692636
TABLE 6 — ClO 2 concentration (ppm)
Lapse timeTemperatureHumidityComparative
(hr)(° C.)(%)Example 3Example 3
150720.0692635
154719.8582634
156319.9632832
157919.9693035
161619.7553034
163519.9563034
165319.9613034
167719.9603034
170119.9583033
172519.9573033
175920.0543033
178320.0573031
180719.8523030
181919.8502630
184319.8522630
186719.7502630
189120.0563032
191820.0553032
194019.8573032
196219.9633031
198619.9512628
201019.9422428
202420.0492628
205720.0402428
208320.1572530
210719.9652530
211520.1702530
213119.9652530
214420.1652529
215519.9652529
217920.0632428
219120.0652428
220320.2492530
221620.0502629
222619.9462529
223919.9482529
225019.9432529
226420.1502529
227520.0522630
228820.1552630
229820.0502528
231220.0452528
232220.1432629
233620.0432529
234620.0402629
236020.0452629
237020.0452629
238420.1512829
239420.0452627
240820.0452627
241819.9442627
243119.9462627
244220.0382527
245520.0502627
246620.050——
247920.0502627
249019.948——
250320.0422427
251420.041——
252720.040——
253820.038——
255120.041——
256220.0362225
257520.040——
258620.0362325
259919.937——
TABLE 7 — ClO 2 concentration
Lapse timeTemperatureHumidity(ppm)
(hr)(° C.)(%)Example 4
0.520.16935
2.020.17135
1920.08025
3020.07925
5220.27940
6820.08050
9120.08648
16320.08646
20920.27544
28120.27945
37720.27445
49720.37847
56920.37849
63120.17551
67920.17550
75120.27744
82320.27435
94320.27243
106320.27943
113520.28040
135120.28738
149520.08438
163920.27234
185520.08433
207119.98032
226320.27932
TABLE 8 — ClO 2 concentration
Lapse timeTemperatureHumidity(ppm)
(hr)(° C.)(%)Example 5
0.520.68439
2.020.67740
2220.08635
3520.28451
4520.08650
6920.08450
11720.08652
16319.88750
23520.27948
30720.27948
42720.27448
52320.37849
64320.37850
69120.17548
73920.07544
83520.27543
97920.27944
111420.27944
128220.28643
140220.28442
161820.28740
183420.27240
197820.08042
214620.07941
233819.95539
TABLE 9 — ClO 2 concentration
Lapse timeTemperatureHumidity(ppm)
(hr)(° C.)(%)Example 6
0.520.68442
2.020.67752
2220.08653
3520.28455
4520.08655
6920.08455
11720.08654
16319.88751
23520.27950
30720.27948
42720.27448
52320.37850
64320.37850
69120.17552
73920.07545
83520.27543
97920.27945
111420.27943
128220.28644
140220.28442
161820.28740
183420.27242
197820.08042
214620.07940
233819.95538

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2 codes
IPC · International Patent Classification
Section B — Performing operations; transporting
  • B01J13/00
Section C — Chemistry; metallurgy
  • C01B11/02

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