CN102847181B - Product capable of delaying generation and releasing of chlorine dioxide and preparation method thereof - Google Patents
Product capable of delaying generation and releasing of chlorine dioxide and preparation method thereof Download PDFInfo
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- CN102847181B CN102847181B CN201210364816.3A CN201210364816A CN102847181B CN 102847181 B CN102847181 B CN 102847181B CN 201210364816 A CN201210364816 A CN 201210364816A CN 102847181 B CN102847181 B CN 102847181B
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Abstract
The invention relates to a product capable of delaying generation and releasing of chlorine dioxide and a manufacture method thereof. The product comprises a porous carrier, chlorite adhered onto the porous carrier and alkaline matters adhered onto the porous carrier. The invention further discloses the method for manufacturing stabilized chlorine dioxide products. The method includes steps of: (a) preparing aqueous solution containing the chlorine dioxide and the alkaline matters; (b) preparing aqueous suspension containing organic hydrocarbon, wherein the aqueous suspension containing the organic hydrocarbon can be prepared independently or be prepared together with the chlorine dioxide and the alkaline matters in solution obtained in the step (a); (c) adding the solution obtained in the step (a) and the step (b) (if the solution is prepared in the step (b)) into the porous carrier, and evenly mixing the solution so as to enable the porous carrier to absorb the chlorine dioxide, the alkaline matters and optional organic hydrocarbon and alkaline salt in the solution.; and (d) drying the mixture obtained in the step (c) to enable the water content to be lower than 10%, and packaging in sealing mode to obtain the product.
Description
Technical field
The present invention relates to a kind of goods that chlorine dioxide produces and discharges that delay, this product can be for environment purification, can also be in the time of transporting food products etc. for smelly eliminating, sterilization, removal virus, mildew-resistant, anticorrosion etc., the present invention relates to the goods of the stabilizing chlorine dioxide using for these objects, and relate to and use this goods/product to make it delay ground, stably produce the method for Low Concentration Chlorine Dioxide gas.
Background technology
Chlorine dioxide is a kind of strong oxidizer, in the purposes of smelly eliminating, sterilization, removal virus, mildew-resistant, anticorrosion, bleaching etc., has been considered to good prospect.But due to very unstable of chlorine dioxide, be not suitable for long-term storage and transport, and have the problems such as explosion danger when high concentration, in order to address these problems, people attempt having used many methods.
For example, and CN1915041A (Chinese Patent Application No.: 200610030912.9, open day: 2007-2-21) disclose a kind of vegetable, fruit antistaling agent goods and application thereof, these goods activate chlorine dioxide (ClO by 5000ppm
2) account for constituent gross weight 30～40%, ultra-fine Ore powder 20～30% and the Gleditsia officinalis rubber powder that account for constituent gross weight account for 40% of constituent gross weight and form, then add water and diluted.Described activation chlorine dioxide (ClO
2) be universally acknowledged nontoxic, harmless disinfectant; Ultra-fine Ore powder is taken from smectite, meerschaum, zeolite, limestone, the Maifanitum of occurring in nature, the particulate material of porous rock, then through superfine grinding processing, its particle diameter is between 0.001-0.0001mm; The natural gum powder refining in Gleditsia officinalis seed.Vegetable, fruit antistaling agent that these three kinds of materials are consisted of the dilution of 50-100 times of water, sterilization, sterilization, parasite killing, insect protected, the inhibition that can solve fruit and vegerable breathe, eliminate second rare, reduce moisture loss, nutrient consumption, prevent variable color, the problem such as spoiled, rotten.Can accomplish again the advantages such as harmless, nontoxic, nonpollution environment, low cost, easy to use, easy operation.
Although for example, by making stabilizing chlorine dioxide and water-absorbing resins form the scheme (, referring to JP 61-181532 communique) of spawn,, there is the problems such as chlorine dioxide that substantially do not produce in the method.In order to address this problem, for example, although the method for the spawn being made up of with ultraviolet radiation chlorine dioxide and water-absorbing resins proposition (, referring to JP 2000-202009 communique), but this method must combine with ultraviolet lamp.
Propose in order to chlorine dioxide lysate although have, chlorite and maintain acid ph adjusting agent be composition pure chlorine dioxide goods, and the gel constituent that contains super absorbent resin (for example, referring to Unexamined Patent 11-278808 communique), but due to the decomposition of chlorine dioxide lysate, be not suitable for long-term preservation.
In addition, propose to add activator in chlorite aqueous solution although have, water-absorbing resins and water-retaining agent the method that makes its gelation are (for example, referring to JP 2007-1807 communique), but, during due to use, must add medicament, exist the reaction after adding uncontrollable, after interpolation, a few days all produces the problem of the chlorine dioxide of high concentration.
Therefore, the method that can make chlorine dioxide stable that provides is expected to have in this area, expects that the method can delay chlorine dioxide and from product, produces and discharge.
Summary of the invention
The object of the present invention is to provide a kind ofly can make the stable method of chlorine dioxide, expect that the method can delay chlorine dioxide and from product, produces and discharge.The inventor finds, in porous carrier, flood chlorite and specific material, can obtain stabilizing chlorine dioxide goods/product, this product can be by chlorine dioxide for environment purification, or in the time of transport food smelly eliminating, sterilization, except virus, mildew-resistant, anticorrosion aspect, provide while preservation and do not produce chlorine dioxide, but can delay ground in use, stably produce the stabilizing chlorine dioxide goods of chlorine dioxide and allow its stable method that produces chlorine dioxide.
First aspect present invention provide a kind of can delay ground, the goods of chlorine dioxide are stably provided, it comprises porous carrier, be attached to chlorite on this porous carrier, be attached to the alkaline matter on this porous carrier.
According to the goods of first aspect present invention, wherein said porous carrier is selected from meerschaum, Paligorskite, Montmorillonitum, silica gel, kieselguhr, zeolite, perlite, active carbon.The porous carrier using in stabilizing chlorine dioxide goods in the present invention, although can use meerschaum, Paligorskite, Montmorillonitum, silica gel, kieselguhr, zeolite, perlite, active carbon etc., but for chlorite is not decomposed, while being suspended, be alkaline carrier relatively good in water, Paligorskite is just relative better with meerschaum, and wherein meerschaum is best.Meerschaum is the natural mineral matter of britesorb, and chemical constitution formula is as follows.
(OH
2)
4(OH)
4Mg
8Si
12O
30·8H
2O
This crystal structure surface is fibrous, and when surperficial many ditches, there is the space of a lot of cylindrical tunnel constructions inside, is the very large material of surface area.In the present invention, no matter be that meerschaum tcrude ore is pulverized refining material afterwards, or the meerschaum after moulding, or the material of any shape of granular, the powdery that is that calcining obtains in 100-800 ° of C, fibrous, molded body, can use according to purposes.In addition, the absorption water holding capacity of meerschaum is very big, can present dry state even absorb with the moisture of self identical weight.
According to the goods of first aspect present invention, wherein said chlorite can be chlorous alkali metal salt or chlorous alkali salt.The chlorite that the present invention uses, specifically, the alkali metal salt that can exemplify out has sodium chlorite, potassium chlorite, lithium chlorite etc., is best from economy and practicality sodium chlorite.In the time of preparation stabilizing chlorine dioxide goods of the present invention, the chloritic concentration using, typically 1 % by weight is effective above, but exceed 25 % by weight and be not suitable for producing manipulation later, so make chlorite be attached to porous carrier in time, its concentration is generally 1 % by weight ~ 25 % by weight, and more generally 5% ~ 20%.Although people expect for the porous carrier of fixed amount, chlorite adsorbance is more conducive to more greatly the use of goods of the present invention, but the object of the invention is to make chlorite to be more stably attached on porous carrier, thereby the size of chlorite adsorbance is not that the inventor pays close attention to, the inventor expects to adsorb chloritic amount on 1000g porous carrier can be at 1g ~ 500g, for example 10g ~ 250g, for example 25g ~ 250g, for example 50g ~ 250g, for the object of the invention, without chloritic adsorbance on porous carrier is particularly limited.
According to the goods of first aspect present invention, wherein said alkaline matter can be organic base or inorganic base, preferably inorganic base.The alkaline matter using in the present invention can be for example sodium hydroxide, potassium hydroxide, Lithium hydrate, sodium carbonate, potassium carbonate, lithium carbonate etc.Passable from the viewpoint of economic sodium hydroxide and sodium carbonate, from the storage stability of stabilizing chlorine dioxide goods, sodium hydroxide is better.
According to the goods of first aspect present invention, wherein said alkaline matter mole is 0.1 ~ 1:1 with the ratio (R1) of chlorite mole, for example 0.1 ~ 0.7:1, for example 0.1 ~ 0.6:1.In 0.1 times of amount of less than, the chlorite of absorption easily decomposes at normal temperatures, although improved stability when exceeding 0.7, is difficult to produce chlorine dioxide, not ideal.
Stabilizing chlorine dioxide goods in the present invention are in porous carrier, to flood chlorite and alkali and make its material dry and that obtain, and dry degree (moisture content) has great impact to the performance of stabilizing chlorine dioxide goods.That is to say the high decomposition reaction that can promote chlorite generation chlorate of moisture content of stabilizing chlorine dioxide goods.In addition, although also do not have the chlorine dioxide clearly whether generating to be blocked by moisture, the chlorine dioxide that the words that water content is high produce just tails off.In general, in stabilizing chlorine dioxide goods of the present invention, water content is preferred below 10 % by weight, and also can be suitable for the great majority use situation of goods of the present invention, water content is preferred below 7.5 % by weight, and water content is more preferred below 5 % by weight.Due to the carrier mass of stabilizing chlorine dioxide goods of the present invention be have porous, it is after having adsorbed chlorite and alkaline matter, can easily remove moisture wherein by conventional intensification dry run, and the water quantities reaching below 5 % by weight is easy to those skilled in the art.Therefore, for purposes of the present invention, stabilizing chlorine dioxide goods of the present invention need not be particularly limited moisture wherein, and in case of no particular description, the water content in these stabilizing chlorine dioxide goods is below 10 % by weight, below 7.5 % by weight or below 5 % by weight.
In addition, have been surprisingly found that, in stabilizing chlorine dioxide goods preparation process of the present invention, add appropriate basic salt particularly the basic salt of mineral acid can to make to be adsorbed on chlorite on carrier more stable.Above-mentioned basic salt is such as but not limited to phosphate, sulfate and carbonate, for example sodium phosphate, sodium hydrogen phosphate, sodium sulfate, sodium carbonate.Preferably basic salt is sodium phosphate and sodium hydrogen phosphate, and preferred basic salt is sodium phosphate.Especially, in the time adding basic salt, basic salt mole is 0.01 ~ 0.5:1 with the ratio (R2) of chlorite mole, for example 0.01 ~ 0.25:1, for example 0.01 ~ 0.1:1.Above-mentioned basic salt can together add with for example sodium hydroxide of alkaline matter, can also before alkaline matter adds or after alkaline matter adds, feed intake.Overall and it all can add under the condition that can evenly add, for example before bone dry, do not add basic salt there being enough water yields, therefore the mode that adds of basic salt can not be subject to special restriction in the present invention.
In addition, also have been surprisingly found that, in stabilizing chlorine dioxide goods preparation process of the present invention, add appropriate organic hydrocarbon compound can make to be adsorbed on chlorite on carrier more stable.Esters, aliphatic alcohols and fatty acid that above-mentioned organic hydrocarbon generates such as but not limited to paraffinic, chain alkene, fatty alcohol and aliphatic carboxylic acid.In one embodiment, described organic hydrocarbon is the organic hydrocarbon that comprises 16 ~ 20 carbon.In one embodiment, described organic hydrocarbon is the organic hydrocarbon that comprises 16 or 18 carbon.In one embodiment, described organic hydrocarbon is straight-chain hydrocarbons.In one embodiment, described organic hydrocarbon is saturated hydrocarbons.In one embodiment, described organic hydrocarbon is selected from hexadecanol, octadecanol, 16 octadecanols, hexadecane, octadecane, stearic acid, stearate for example magnesium stearate, sodium stearate and combination thereof.Especially, in the time adding organic hydrocarbon, the weight of organic hydrocarbon is 0.01 ~ 0.5:1 with the ratio (R3) of chlorite weight, for example 0.01 ~ 0.2:1.Above-mentioned organic hydrocarbon can together add with for example sodium hydroxide of alkaline matter, can also before alkaline matter adds or after alkaline matter adds, feed intake.Overall and it all can add under the condition that can evenly add, for example before bone dry, do not add organic hydrocarbon there being enough water yields, therefore the mode that adds of organic hydrocarbon can not be subject to special restriction in the present invention.In addition, adding fashionablely together with alkaline matter, the dissolubility of organic hydrocarbon may be more not enough, now can add wherein in the mode of suspendible.
According to the goods of first aspect present invention, its in water when suspendible aqueous solution be shown as alkalescence.
According to the goods of first aspect present invention, wherein said porous carrier is Paligorskite or meerschaum.
According to the goods of first aspect present invention, wherein moisture is below 5%.
Second aspect present invention provides the method for preparing stabilizing chlorine dioxide goods described in first aspect present invention, and it comprises the following steps:
(a) aqueous solution that preparation comprises chlorite and alkaline matter;
(b) aqueous suspensions that preparation comprises organic hydrocarbon, the aqueous suspensions of this organic hydrocarbon can be prepared separately, or is formulated in together with alkaline matter with chlorite in the solution of step (a);
Optionally (b ') prepare the aqueous solution that comprises basic salt, this base brine solution can be prepared separately, or is formulated in together with alkaline matter with chlorite in the solution of step (a);
(c) to the solution that adds step (a) and step (b) (if present) and optional step (b ') (if present) gained in porous carrier, mix homogeneously, so that chlorite, alkaline matter and optional organic hydrocarbon and the basic salt in porous carrier adsorbent solution;
(d) make step (c) gained mixture dry, make water content lower than 10%, pack, to obtain final product.
According to the method for second aspect present invention, wherein said porous carrier is selected from meerschaum, Paligorskite, Montmorillonitum, silica gel, kieselguhr, zeolite, perlite.In one embodiment, described porous carrier is meerschaum.In the present invention; described meerschaum can be that powder after meerschaum Ore is directly pulverized or granule or its article shaped (are former powder or granule form definite shape material through processing; for example graininess, bulk), that can also to be meerschaum Ore obtain through 100-800 ° of C calcining is granular, powdery, fibrous or its article shaped.
According to the method for second aspect present invention, wherein said chlorite can be chlorous alkali metal salt or chlorous alkali salt, for example sodium chlorite, potassium chlorite, lithium chlorite.
According to the method for second aspect present invention, wherein in step (a), chloritic concentration is 1 % by weight ~ 25 % by weight, for example 5 % by weight ~ 25 % by weight, preferably 5% ~ 20%.
According to the method for second aspect present invention, wherein said alkaline matter can be organic base or inorganic base, preferably inorganic base, such as sodium hydroxide, potassium hydroxide, Lithium hydrate, sodium carbonate, potassium carbonate, lithium carbonate etc.
According to the method for second aspect present invention, esters, aliphatic alcohols and fatty acid that wherein said organic hydrocarbon generates such as but not limited to paraffinic, chain alkene, fatty alcohol and aliphatic carboxylic acid.In one embodiment, described organic hydrocarbon is the organic hydrocarbon that comprises 16 ~ 20 carbon.In one embodiment, described organic hydrocarbon is the organic hydrocarbon that comprises 16 or 18 carbon.In one embodiment, described organic hydrocarbon is straight-chain hydrocarbons.In one embodiment, described organic hydrocarbon is saturated hydrocarbons.In one embodiment, described organic hydrocarbon is selected from hexadecanol, octadecanol, hexadecane, octadecane, stearic acid, stearate for example magnesium stearate, sodium stearate and combination thereof.
According to the method for second aspect present invention, wherein the amount ratio (R1) of step (a) neutral and alkali material mole and chlorite mole is 0.1 ~ 1:1, for example 0.1 ~ 0.7:1, for example 0.1 ~ 0.3:1.
According to the method for second aspect present invention, wherein said basic salt is such as but not limited to phosphate, sulfate and carbonate, for example sodium phosphate, sodium hydrogen phosphate, sodium sulfate, sodium carbonate.Preferably basic salt is sodium phosphate and sodium hydrogen phosphate, and preferred basic salt is sodium phosphate.
According to the method for second aspect present invention, the amount that wherein step (a) or step (b ') neutral and alkali salt uses is counted with respect to chlorite, particularly the mole of basic salt and the amount ratio of chloritic mole (R2) are 0.01 ~ 0.5:1, for example 0.01 ~ 0.25:1, for example 0.05 ~ 0.2:1.
According to the method for second aspect present invention, the amount that wherein in step (a) or step (b), organic hydrocarbon uses is counted with respect to chlorite, particularly, in the time adding organic hydrocarbon, the weight of organic hydrocarbon is 0.01 ~ 0.5:1 with the ratio (R3) of chlorite weight, for example 0.01 ~ 0.2:1.
According to the method for second aspect present invention, wherein step (d) dry is to make in stabilizing chlorine dioxide goods that the present invention obtains water content below 10 % by weight, water content is preferred below 7.5 % by weight, and water content is more preferred below 5 % by weight.
Third aspect present invention provides the method that produces and/or discharge chlorine dioxide in substantially controlled mode, and the method comprises the following steps:
(i) provide the stabilizing chlorine dioxide goods described in the arbitrary embodiment of first aspect present invention, before using, these goods being wrapped in to packaging material (the being barrier material) container that can completely cut off moisture and circulation of air can be for example in sack, so that these goods did not substantially produce and/or discharge chlorine dioxide before using;
(ii) in the time using these goods, described container is opened, to allow that the moisture outside container contacts with these goods with air, and produced and/or release chlorine dioxide.
According to the method for third aspect present invention, wherein open the mode of described vessel port size by control, to control moisture and air and the amount that these goods contact, control the speed that chlorine dioxide produces and/or discharges.
Arbitrary technical characterictic that arbitrary embodiment of either side of the present invention or this either side has is suitable for arbitrary embodiment of other arbitrary embodiment or other either side equally, as long as they can be not conflicting, certainly, at where applicable each other, necessary words can be done suitably to modify to individual features.Be further described with feature to various aspects of the present invention below.
All documents that the present invention quotes from, their full content is incorporated to herein by reference, and if when the expressed implication of these documents and the present invention are inconsistent, be as the criterion with statement of the present invention.In addition, various terms and phrase that the present invention uses have the general sense of well known to a person skilled in the art, nonetheless, the present invention still wishes at this, these terms and phrase to be described in more detail and to be explained, the term of mentioning and phrase, if any inconsistent with known implication, are as the criterion with the implication that the present invention was explained.
Be further described to various aspects of the present invention below.
In the present invention, unless otherwise noted, % is the percent of w/w.
In the present invention, term " stabilizing chlorine dioxide goods " refers to a kind of artifact, and it can control the release of chlorine dioxide substantially by the demand of people's expection.Because chlorine dioxide can be reacted and form with carbon dioxide and water by chlorite, the present invention is by being attached on porous carrier chlorite, thus obtained product, be referred to as " stabilizing chlorine dioxide goods ", its with surrounding air in water and carbon dioxide contact process in chemically reactive and discharge that chlorine dioxide is this can be for the gas of the purposes such as sterilization, therefore the present invention " stabilizing chlorine dioxide goods " can also be called a kind ofly can make chlorine dioxide-based the upper artificial manufactured goods with expection object Stable Release.
In the present invention, term " porous carrier " is a kind of absorption carrier, and it is because of the high chlorite that can efficient adsorption can decompose chlorine dioxide of porosity.The apparent shape of porous carrier is not particularly limited, and for example it can be graininess, Powdered, block etc.
In the present invention, term " is attached to the chlorite on this porous carrier " and refers to because porous carrier inside exists all concrete dynamic modulus, chlorite can be attached to these pore surfaces, and the larger area that can adsorb for chlorite of pore surface area of porous carrier inside is just larger.Equally similarly, term " is attached to the alkaline matter on this porous carrier " also similar meaning.
In the present invention, " water content " of stabilizing chlorine dioxide goods of the present invention refers to the water quantities comprising in manufactured goods of the present invention, these moisture normally manufactured goods are difficult to remove completely in dry run, for example, when water quantities is reduced to below 5%, continue to reduce its cost of water quantities will increase greatly again.But at product scope of the present invention, in order to control chlorite decomposition, water quantities is lower than the normally acceptable of stabilizing chlorine dioxide goods of the present invention of 7.5 % by weight.
In the present invention, when stabilizing chlorine dioxide goods of the present invention are packed, conventionally employing can completely cut off the packaging material of moisture and circulation of air, it can be called barrier material, for example sack of packing container or for example plastic bottle or vial that such as clad aluminum plastic film, extrusion coating paper plastic film etc. form, this type of packing container can for stabilizing chlorine dioxide goods of the present invention provide good storage, transportation environment not can with airborne moisture and air sustained response, decomposition.In the time that stabilizing chlorine dioxide goods of the present invention need to use, can open the above-mentioned packing container material that can completely cut off moisture and circulation of air.Certainly, in the above-mentioned packing container inside that can completely cut off moisture and circulation of air of the present invention, can also comprise such as packing inside bag of an inner container, it is can allow to be moisture and the air of gaseous state and to decompose the chlorine dioxide producing to pass in and out such as packing inside bag of this inner container, and the stabilizing chlorine dioxide goods of the present invention that are still granule, powder or other state but can not freely pass through such as packing inside bag of this inner container.Like this, in the time that stabilizing chlorine dioxide goods of the present invention use, open the such as packing inside bag of inner container being formed by insulation layer, be that the moisture of gaseous state and air can pass through inner packaging material and the hole inside that enters stabilizing chlorine dioxide goods of the present invention, and react with the chlorite wherein adhering to, generate Chlorine Dioxide Gas and from inner packaging material, escape in external environment condition, for purposes such as sterilizations.
In the process of preparation stabilizing chlorine dioxide goods of the present invention, basic salt can be prepared separately, can also be formulated in same solution with chlorite and alkaline matter.
In the process of preparation stabilizing chlorine dioxide goods of the present invention, organic hydrocarbon can be prepared separately, can also be formulated in same solution with chlorite and alkaline matter and optional basic salt.
In the process of preparation stabilizing chlorine dioxide goods of the present invention, moisture drying is left to the process of porous carrier, this dry run can be the combination of natural air drying, drying under reduced pressure, heat drying etc. or these drying meanss.Because porous carrier water absorbing capacity of the present invention is quite strong, it absorbs after the aqueous solution of a large amount of dissolving chlorites and alkaline matter and basic salt, outward appearance still can be dry or partial desiccation state, and therefore follow-up dry run easily realizes by natural air drying, drying under reduced pressure.Certainly, say from production efficiency, heat drying can be adopted conventionally.Typically, in the time of preparation product of the present invention, heat drying temperature used is usually less than 100 ° of C, more generally lower than 80 ° of C, and for example approximately 50 ° of C, approximately 60 ° of C, approximately 70 ° of C, approximately 80 ° of C.It will be appreciated by those skilled in the art that what drying process of the present invention was normally dried at the temperature of 50 ° of C to 80 ° of C.
In the present invention, in porous carrier, flood chlorite and alkali, and to make it dry be the feature of stabilizing chlorine dioxide goods.The porous carrier using is alkalescence in being suspended in water.Use the concentration of alkali for every mol chlorite, higher than 0.1 times of amount lower than 0.7 times of amount.Below water quantities 10 % by weight in these stabilizing chlorine dioxide goods.In addition, these stabilizing chlorine dioxide goods will completely cut off carbon dioxide and steam when preservation, and when use, allowing it contact with carbon dioxide and steam is to make its stable feature that produces chlorine dioxide body method.
In the present invention, to utilize chlorine dioxide environment purification or the smelly eliminating when the food transport, sterilization, remove virus, mildew-resistant, anticorrosion is object, and the stabilizing chlorine dioxide goods of the stable generation chlorine dioxide of (neither too much nor too little) are in right amount provided, particularly with provide preserve time do not produce chlorine dioxide, the method that produces chlorine dioxide when use is object.
In the present invention, to porous carrier dipping chlorite and alkaline matter dry and in the stabilizing chlorine dioxide goods that obtain, use the amount of alkali for every mol chlorite, higher than 0.1 times of amount lower than 0.7 times of amount.Dried moisture amount is the stabilizing chlorine dioxide goods below 10 % by weight.
In the present invention, in preserving stabilizing chlorine dioxide goods, making its isolated carbon dioxide and steam, is the stable method that produces chlorine dioxide by making carbon dioxide in its ingress of air and steam produce chlorine dioxide when use.
Stabilizing chlorine dioxide goods of the present invention, generation chlorine dioxide that can be stable in right amount, in addition, by the method for generation chlorine dioxide of the present invention, does not produce chlorine dioxide can accomplish to preserve time, just produce chlorine dioxide when use.Further, utilize the chlorine dioxide production method of stabilizing chlorine dioxide goods of the present invention, in preserving, do not produce chlorine dioxide, be applicable to long-term preservation and carrying, when use, can stablize and produce chlorine dioxide, the danger of blast is very low, and this is quite satisfactory.
In addition, stabilizing chlorine dioxide goods of the present invention, it is the mode of appearance of the present invention's porous carrier used substantially, i.e. the form of powder, granule or block.These forms are quite favourable for disposal process such as the production of product, transportation, uses.
In the present invention, stabilizing chlorine dioxide goods just refer to the material of energy stable releasing chlorine dioxide, and it is to porous carrier inner dipping chlorite and alkaline matter dried material.
In the present invention, stabilizing chlorine dioxide goods, are to mix add the porous carrier being fully dried in the mixed liquor of chlorite aqueous solution and alkali and optional basic salt and hydrocarbon after, dry; Or add after mixed base to porous carrier, then add and mix dry after chlorite aqueous solution and obtain.In addition, can obtain the chloritic stabilizing chlorine dioxide goods of high-load by aforesaid operations repeatedly.Drying means and equipment are not particularly limited, vacuum drier, and flowing dryer, goods-shelf type drying machine, Clothoid type drying machine etc. can.
Produced in the present invention the method for chlorine dioxide by stabilizing chlorine dioxide goods, enumerate and allowed stable chlorine dioxide goods with the method for acidic materials or oxidizing substance mixing and the method that allows stabilizing chlorine dioxide goods contact with air, make the stable generation of chlorine dioxide and within the regular hour, discharging in this point, the method that allows stabilizing chlorine dioxide goods contact with air is good.
In the present invention, by the method that allows chlorine dioxide goods contact with air, can produce chlorine dioxide.Therefore, inventors of the present invention, compared to passing into common air in chlorine dioxide goods of the present invention, pass into by sodium hydrate aqueous solution removed carbon dioxide air, pass into the generation (seeing below) of having been removed the chlorine dioxide under these three kinds of methods of air of carbon dioxide and steam by sodium hydrate aqueous solution and calcium chloride.Compared with passing into normal air, while passing into the air of removing carbon dioxide, the generation of chlorine dioxide greatly reduces, and while passing into the air of removing carbon dioxide and steam, the generation of chlorine dioxide is 0 substantially.Can think that this is because steam and carbon dioxide produce carbonic acid after being absorbed by the hole of stabilizing chlorine dioxide goods as following chemical equation, because carbonic acid is the first weak acid that dissociates fixed number pk1=6.4, this carbonic acid is as acid and chlorous acid salt face effect and produce chlorine dioxide.
CO
2+2H
2O→H
2CO
3
By this phenomenon, do not need same acidic materials to mix, contact and can produce chlorine dioxide with steam with definite the saying with airborne carbon dioxide of air contact.Otherwise, by avoiding same carbon dioxide to contact the generation that just can suppress chlorine dioxide with steam.Therefore, while use, chlorine dioxide goods are packed in the container that is difficult to see through carbon dioxide and steam material, or the generation of chlorine dioxide while suppressing not use by the method such as pack, when use, contact with ambient atmos and (take out from container by it, open container cover, take out packaging material etc.) and slowly discharge chlorine dioxide.
To calcining under 700 ° of C in sepiolite particle (particle diameter 1-3mm) 81kg forming for 3 hours, add contain 25% sodium chlorite and 25% sodium hydroxide aqueous solution (containing amount sodium chlorite in this aqueous solution is that 16kg, amount of sodium hydroxide are 1kg) afterwards, vacuum drying 5 hours under 70 ° of C, obtaining absorption has the goods of the discharged chlorine dioxide of sodium chlorite, these goods are by dry its moisture of measuring of 105 ° of C, and moisture is approximately 2%.The chlorine dioxide goods 40g obtaining is thus put in the packed tower (diameter 50 × high 150mm) of 300ml glass system, at 25 ° of C of temperature, under humidity 60% condition, pass into the normal air (gas 1) of 5 hours with the speed of 1L/min, pass into the air (gas 2) of being removed carbon dioxide by 25% sodium hydrate aqueous solution, pass into the air (gas 3) of being removed carbon dioxide and steam by 25% sodium hydrate aqueous solution and calcium chloride tube, measure the generation of the chlorine dioxide under these 3 kinds of methods.Result shows, (gas 1 when passing into common air, gas generated is 10mg/hr/kg) compare, when passing into the air of removing carbon dioxide, the generation of (gas 2, gas generated is 3mg/hr/kg) chlorine dioxide significantly reduces; When passing into the air of removing carbon dioxide and steam (gas 3, gas generated is 0.15mg/hr/kg), the generation of chlorine dioxide can be suppressed at below 0.2% substantially.
In the present invention, sodium chlorite method for detecting purity can (can be described as iodimetry) with the following method in the present invention:
Reagent and solution: 1, sulfuric acid solution (1+8): draw 20mL sulphuric acid, slowly add in 160mL water, constantly stir.
2, liquor kalii iodide (100g/L): take 20g potassium iodide, dissolve in 200mL water, newly join.
3, starch indicator solution (5g/L): take starch 0.5g, dissolve in 100mL boiling water, newly join.
4, sodium thiosulfate standard solution [c (Na
2s
2o
3)=0.100mol/L]: take 26g sodium thiosulfate and 0.2g sodium carbonate, add the appropriate cold water newly boiling to make it to dissolve, and be diluted to 1000mL, mix, proceed in brown reagent bottle, place after one month and filter, for subsequent use after accurate calibration.
The demarcation of sodium thiosulfate standard solution: precision takes about 0.15g and be dried at 120 ° of C the potassium dichromate (national standard material GBW 06105c) of constant weight, is placed in 500mL iodine flask, adds 50mL water to make it to dissolve.Add 2g potassium iodide, jolting makes it to dissolve gently, then adds 20mL sulfuric acid solution (1), airtight, shakes up.After being put in dark place 10min, use the dilution of 250mL water.Drip to solution with sodium thiosulfate titrand and be faint yellow, then add 3mL starch indicator solution (3), continue to be titrated to blueness and disappear and highlight green.The temperature of reactant liquor and thinned water should be higher than 20 ℃.Carry out reagent blank test simultaneously.
Determination step: weigh the sample being equivalent to containing the 3g sodium chlorite of having an appointment, be accurate to 0.0002g, be placed in 100mL beaker, after being dissolved in water, all move in 500mL volumetric flask, be diluted with water to scale, shake up.
Measure 10mL test solution, be placed in the 250mL iodine flask of the liquor kalii iodide (2) that is added with in advance 20mL, add 20mL sulfuric acid solution (1), shake up.Place 10min in dark place.Add 100mL water, when being titrated to solution and being light yellow with sodium thiosulfate standard solution (4), add about 3mL starch indicator solution (3), continue to be titrated to blue disappearance and be terminal, do blank assay simultaneously.Calculate the content of sodium chlorite in sample.The difference of twice parallel assay result is not more than 0.2%, and getting its arithmetic mean of instantaneous value is measurement result.
In addition, sodium chlorite purity/detection method of content is also to carry out with reference to the method for recording in the chemical industry standard HG3250-2001 of the People's Republic of China (PRC).
Because stabilizing chlorine dioxide goods related to the present invention can be during certain in the chlorine dioxide of generation stable quantity, so be suitable as very much the uses such as antibacterial, deodorant, antiseptic and antifungus agent.
The transmitance of the packaging material that the method for stable generation chlorine dioxide of the present invention is used or the carbon dioxide of container and steam is as following institute example.The transmitance of carbon dioxide is preferably controlled at 2.5 × 10
-11cc (STP)/cm
2below seccmHg, if thickness is the packaging film of 50 μ m, be controlled at 5 × 10
-11cc (STP)/cm
2seccmHg is good below.In addition, the transmitance of steam is preferably controlled at 5 × 10
-9cc (STP)/cm
2below seccmHg, if thickness is the packaging film of 50 μ m, be controlled at 1000 × 10
-10cc (STP)/cm
2seccmHg is good below.The material that makes carbon dioxide and steam be difficult to see through was considered metal, glass etc., during particularly as packaging material and container cover use, plastic film is widely used, and in that case, can use vacuum aluminum-coated polyethylene film, vinylidene chloride, polytrifluorochloroethylene etc.
The specific embodiment
Further illustrate the present invention below by specific embodiment/experimental example, still, should be understood to, these embodiment and experimental example are only used for the use specifically describing more in detail, and should not be construed as for limiting in any form the present invention.
The present invention carries out generality and/or concrete description to the material and the test method that use in test.Although be well known in the art for realizing many materials and the operational approach that the object of the invention uses, the present invention still does to describe in detail as far as possible at this.It will be apparent to those skilled in the art that hereinafter, if not specified, material therefor of the present invention and operational approach are well known in the art.
In the product that test obtains below, when they are completely cut off to packing of carbon dioxide and aqueous vapor, if not otherwise indicated, the isolated carbon dioxide using and the packaging material of aqueous vapor are vacuum aluminum-coated polythene film bags, and allow that the inner packaging material that is moisture and the air of gaseous state and decomposes the chlorine dioxide turnover producing is non-woven bag; If not otherwise indicated, every bag of dispensed loading amount is 50 grams.Hereinafter, if not otherwise indicated, the meerschaum using is that sepiolite that Neixiang County, Henan Province produces is calcined 3 hours and the granule made under 700 ° of C, particle diameter 1-3mm.
embodiment 1:
To calcining under 700 ° of C in the meerschaum (particle diameter 1-3mm) forming for 3 hours, (be mixed with in advance aqueous solution in following ratio interpolation sodium chlorite and sodium hydroxide, concentration is respectively 25%), mix and make after absorption evenly, vacuum drying 5 hours under 70 ° of C, (in form, the unit of each numerical value is weight portion, in most cases also can be regarded as percetage by weight to obtain the chlorine dioxide goods 1A to 1G of composition as follows; In NaOH hurdle bracket, numerical value is with respect to NaClO
2the mole of alkali, for example, in goods 1A, take every 1 mole of NaClO as 8 weight portions
2meter, the mole of NaOH is 0.14; Water content in numeric representation end article in water hurdle, shows that the water content in goods 1G reaches 15 weight portion/107 weight portions).
| NaClO 2 | NaOH | Water | Meerschaum | |
| Goods 1A | 8 | 0.5(0.14) | 2 | 89.5 |
| Goods 1B | 16 | 1(0.14) | 2 | 81 |
| Goods 1C | 16 | 1(0.14) | 4 | 79 |
| Goods 1D | 16 | 4(0.56) | 2 | 78 |
| Goods 1E | 16 | 0.5(0.07) | 2 | 81.5 |
| Goods 1F | 16 | 8(1.12) | 2 | 74 |
| Goods 1G | 16 | 1(0.14) | 15 | 75 |
By the airtight sample bottle of putting into glass system of the each 10g of stabilizing chlorine dioxide goods goods 1A to 1G, 45 ° of C of temperature, humidity is placed 3 months for 75% time, utilize iodimetry to analyze the concentration of the forward and backward sodium chlorite of high-temperature process, calculate goods after high-temperature process, for the sample without high-temperature process, the percent that wherein sodium chlorite concentrations changes, sodium chlorite concentrations percent change=high-temperature process sample sodium chlorite concentrations is divided by being multiplied by 100% without high-temperature process sample sodium chlorite concentrations.The results are shown in following table.
In addition, each the stabilizing chlorine dioxide goods of preparation above 40g is dropped in the packed tower (diameter 50 × high 150mm) of 300ml glass system, 25 ° of C of temperature, humidity passes into the air of 5 hours 60% time with the speed of 1L/min, the gas of outlet passes into be adjusted in the liquor kalii iodide of pH=7 with phosphate buffer, because chlorine dioxide can make its iodine that dissociates, carry out iodometric titration and can calculate the generation of chlorine dioxide with hypo solution, result is as shown in the table.Measurement unit is the chlorine dioxide that 1kg stabilizing chlorine dioxide goods produce, and represents with mg/hr.
| Sample | Sodium chlorite concentrations percent change | Gas generated (mg/hr/kg) |
| Goods 1A | 93.2% | 7.3 |
| Goods 1B | 91.7% | 8.9 |
| Goods 1C | 94.1% | 8.2 |
| Goods 1D | 95.2% | 7.1 |
| Goods 1E | 29.4% | 30.8 |
| Goods 1F | 93.8% | 0.53 |
| Goods 1G | 26.6% | 4.2 |
Result demonstration, after the amount of sodium hydroxide reduces, the sodium chlorite in goods can not more stably remain in adsorbing material; In addition, it is also unfavorable to sodium chlorite when the water content in goods is higher.Particularly, the chloritic reduction of stabilizing chlorine dioxide goods 1A to 1D and 1F is all below 10%, stabilizing chlorine dioxide goods 1E is because the amount of alkaline matter is decomposed less, stabilizing chlorine dioxide goods 1G causes that because water amount chlorite generates the decomposition reaction of chlorate, and the concentration of sodium chlorite is lower than 1/3 of the initial stage.
In addition, as shown in result in table, stabilizing chlorine dioxide goods 1A to 1D has produced appropriate chlorine dioxide, stabilizing chlorine dioxide goods 1E due to the amount of alkaline matter less and too much generation chlorine dioxide, stabilizing chlorine dioxide goods 1F due to the amount chlorine dioxide deficiencies that produce of alkaline matter more.
Therefore, stabilizing chlorine dioxide goods 1A to 1D of the present invention is compared with stabilizing chlorine dioxide goods 1E to 1G, and 1A to 1D is the appropriate chlorine dioxide of stable generation in can accomplishing during certain.
In other test, the sepiolite of producing using Neixiang County, Henan Province is through being directly ground into fine grained (1 ~ 3mm) as adsorbent, prepare stabilizing chlorine dioxide goods according to said products 1A to 1D method, result shows to have result shown in substantially the same upper table with goods 1A to 1D.In other test, the granule (particle diameter 0.2-1mm) that uses Yi County, Hebei province generation sepiolite to calcine 3 hours under 700 ° of C and to make is as adsorbent, prepare stabilizing chlorine dioxide goods according to said products 1A to 1D method, result shows to have result shown in substantially the same upper table with goods 1A to 1D.In other test, with reference to the preparation technology of goods 1B, be that chloritic dosing concentration is designed to respectively 5%, 10%, 15% and 20%, the concentration of sodium hydroxide arranges identical with sodium chlorite; 4 stabilizing chlorine dioxide goods that obtain thus show to have result shown in substantially the same upper table with goods 1B.
In other test, the granule (particle diameter 0.5-2mm) of calcining 3 hours under 700 °, ore deposit of Paligorskite (palygorskite) C that uses Hebei province to produce and make is as adsorbent, prepare stabilizing chlorine dioxide goods according to said products 1A to 1D method, result shows to have result shown in substantially the same upper table with goods 1A to 1D.
embodiment 2:
To calcining under 700 ° of C in the meerschaum (particle diameter 1-3mm) forming for 3 hours, add sodium chlorite, sodium hydroxide and sodium phosphate in the ratio of weight portion as shown in following table and (be mixed with in advance aqueous solution, concentration is respectively 20%), mix and make after absorption evenly, vacuum drying 5 hours under 70 ° of C, making the water content in goods is 2% (± 0.5%), obtains the chlorine dioxide goods 2A to 2P of composition as follows.The meerschaum that comprises 80 weight portions in each goods of design preparation and the NaClO of 15 weight portions
2.In respectively filling a prescription shown in form, mole deal of numeric representation NaOH for the every 1 molar part sodium chlorite containing in formula in NaOH hurdle; Equally, mole deal of numeric representation sodium phosphate for the every 1 molar part sodium chlorite containing in formula in sodium phosphate hurdle.
By the each 20g of stabilizing chlorine dioxide goods 2A to 2P preparing above, packing into can be by the nonwoven sack of aqueous vapor and air, at 40 ° of C of temperature, humidity is placed 1 month for 60% time, utilize iodimetry to analyze the concentration of the forward and backward sodium chlorite of high-temperature process, calculate goods after high-temperature process, for the sample without high-temperature process, the percent that wherein sodium chlorite concentrations changes, sodium chlorite concentrations percent change=high-temperature process sample sodium chlorite concentrations is divided by being multiplied by 100% without high-temperature process sample sodium chlorite concentrations.The amount ratio (R2) that result is presented at mole and the chloritic mole of basic salt is in the scope of 0.05 ~ 0.2:1, stabilizing chlorine dioxide goods are still can keep the chlorite of high level after high-temperature process, all more than 50%; And when concentration is too low or concentration is higher, chlorite maintenance dose is reduced to below 15%.
| Sample | NaClO 2 | NaOH | Sodium phosphate | Concentration change percent |
| Goods 2A | 15 parts | 0.15mol part | 0mol part | 2% |
| Goods 2B | 15 parts | 0.15mol part | 0.01mol part | 9% |
| Goods 2C | 15 parts | 0.15mol part | 0.05mol part | 58% |
| Goods 2D | 15 parts | 0.15mol part | 0.1mol part | 71% |
| Goods 2E | 15 parts | 0.15mol part | 0.15mol part | 65% |
| Goods 2F | 15 parts | 0.15mol part | 0.2mol part | 55% |
| Goods 2G | 15 parts | 0.15mol part | 0.3mol part | 21% |
| Goods 2H | 15 parts | 0.15mol part | 0.5mol part | 13% |
| Goods 2I | 15 parts | 0.5mol part | 0mol part | 1% |
| Goods 2J | 15 parts | 0.5mol part | 0.01mol part | 6% |
| Goods 2K | 15 parts | 0.5mol part | 0.05mol part | 62% |
| Goods 2L | 15 parts | 0.5mol part | 0.1mol part | 76% |
| Goods 2M | 15 parts | 0.5mol part | 0.15mol part | 71% |
| Goods 2N | 15 parts | 0.5mol part | 0.2mol part | 58% |
| Goods 2O | 15 parts | 0.5mol part | 0.3mol part | 27% |
| Goods 2P | 15 parts | 0.5mol part | 0.5mol part | 11% |
In addition, with reference to above goods 2C, goods 2D, goods 2F, goods 2K, goods 2L, goods 2N, but the basic salt using is sodium hydrogen phosphate, prepare respectively the goods of different formulas, according to method test above, result chlorite concentration change percent all in 50% ~ 75% scope, the goods that for example obtain with reference to goods 2D and goods 2L mode, its chlorite concentration change percent is respectively 64% and 71%.But using sodium hydrogen phosphate as basic salt reference preparation 2B and goods 2H and goods 2J and goods 2P, its chlorite concentration change percent of the goods that obtain is all below 10%.
embodiment 3:
To calcining under 700 ° of C in the meerschaum (particle diameter 1-3mm) forming for 3 hours, add sodium chlorite, sodium hydroxide and organic hydrocarbon compound (according to concentration designing requirement in the ratio of weight portion as shown in following table, make three's dissolution/dispersion in water together), mix and make after absorption evenly, vacuum drying 5 hours under 70 ° of C, making the water content in goods is 2% (± 0.5%), obtains the chlorine dioxide goods 3-1 to 3-18 of composition as follows.The meerschaum that comprises 80 weight portions in each goods of design preparation and the NaClO of 15 weight portions
2.In respectively filling a prescription shown in form, mole deal of numeric representation NaOH for the every 1 molar part sodium chlorite containing in formula in NaOH hurdle; And the weight deal of numeric representation organic hydrocarbon compound for the every 1 weight portion sodium chlorite containing in formula in organic hydrocarbon compound hurdle.
By the each 20g of stabilizing chlorine dioxide goods 3-1 to 3-18 preparing above, packing into can be by the nonwoven sack of aqueous vapor and air, at 40 ° of C of temperature, humidity is placed 1 month for 60% time, utilize iodimetry to analyze the concentration of the forward and backward sodium chlorite of high-temperature process, calculate goods after high-temperature process, for the sample without high-temperature process, the percent that wherein sodium chlorite concentrations changes, sodium chlorite concentrations percent change=high-temperature process sample sodium chlorite concentrations is divided by being multiplied by 100% without high-temperature process sample sodium chlorite concentrations.The amount ratio (R3) that result is presented at amount and the chloritic amount of organic hydrocarbon compound is in the scope of 0.01 ~ 0.2:1, and stabilizing chlorine dioxide goods are still can keep the chlorite of high level after high-temperature process, all more than 45%; And when concentration is too low or concentration is higher, chlorite maintenance dose is reduced to below 20%.
| Sample | NaOH | Octadecanol | Stearic acid | Concentration change percent |
| Goods 3-1 | 0.15 | 0 | 3% | |
| Goods 3-2 | 0.15 | 0.01 | 49% | |
| Goods 3-3 | 0.15 | 0.1 | 67% | |
| Goods 3-4 | 0.15 | 0.2 | 53% | |
| Goods 3-5 | 0.15 | 0.5 | 18% | |
| Goods 3-6 | 0.15 | 1.0 | 11% |
| Goods 3-7 | 0.5 | 0 | 4% | |
| Goods 3-8 | 0.5 | 0.01 | 51% | |
| Goods 3-9 | 0.5 | 0.1 | 71% | |
| Goods 3-10 | 0.5 | 0.2 | 62% | |
| Goods 3-11 | 0.5 | 0.5 | 16% | |
| Goods 3-12 | 0.5 | 1.0 | 7% | |
| Goods 3-13 | 0.25 | 0 | 5% | |
| Goods 3-14 | 0.25 | 0.01 | 47% | |
| Goods 3-15 | 0.25 | 0.1 | 69% | |
| Goods 3-16 | 0.25 | 0.2 | 73% | |
| Goods 3-17 | 0.25 | 0.5 | 18% | |
| Goods 3-18 | 0.25 | 1.0 | 11% |
In addition, with reference to above goods 3-2, goods 3-3, goods 3-4, but the organic hydrocarbon compound using is 16 octadecanols, octadecane or magnesium stearate, prepare respectively the goods of different formulas, according to method test above, result chlorite concentration change percent is all in 45% ~ 75% scope, and for example, with reference to the goods 3-3 goods that for mode, 16 octadecanols, octadecane and magnesium stearate obtain, its chlorite concentration change percent is respectively 61%, 71% and 68%; But the amount ratio (R3) that uses amount and the chloritic amount of these three kinds of organic hydrocarbon compounds is lower than 0.01 or higher than 0.5 o'clock, and chlorite concentration change percent is all lower than 15%.
In addition, in above goods 3-2, goods 3-3, goods 3-4, goods 3-8, goods 3-9, goods 3-10, goods 3-14, goods 3-15, goods 3-16, (mole that it adds and the amount ratio of chloritic mole (R2) are 0.1:1, and result shows that chlorite concentration change percent is all high more than 10% than the corresponding formula that does not add this basic salt to add basic salt sodium phosphate; For example, while adding the sodium phosphate of R2=0.1:1 in goods 3-3, resulting product chlorite concentration change percent is 81%.
Claims (1)
1. can delay ground, the goods of chlorine dioxide are stably provided, it comprises porous carrier, be attached to chlorite on this porous carrier, be attached to the alkaline matter on this porous carrier, and organic hydrocarbon compound and basic salt; Wherein:
Described porous carrier is selected from: meerschaum, Paligorskite, Montmorillonitum, silica gel, kieselguhr, zeolite, perlite, active carbon,
Described chlorite is sodium chlorite,
Described alkaline matter is selected from: sodium hydroxide, potassium hydroxide,
Described organic hydrocarbon compound is selected from: esters, aliphatic alcohols and fatty acid that paraffinic, chain alkene, fatty alcohol and aliphatic carboxylic acid generate,
Described basic salt is selected from: sodium phosphate, sodium hydrogen phosphate;
On every 1000g porous carrier, adsorbing chloritic amount is 10g ~ 250g, the mole of alkaline matter is 0.1 ~ 1:1 with the ratio of chloritic mole, the weight of organic hydrocarbon is 0.01 ~ 0.2:1 with the ratio of chlorite weight, and the mole of basic salt is 0.05 ~ 0.2:1 with the ratio of chloritic mole.
2. according to the goods of claim 1, wherein said porous carrier is selected from meerschaum, Paligorskite.
3. according to the goods of claim 1, wherein on every 1000g porous carrier, adsorbing chloritic amount is 50g ~ 250g.
4. according to the goods of claim 1, wherein said alkaline matter is sodium hydroxide.
5. according to the goods of claim 1, the mole of wherein said alkaline matter is 0.1 ~ 0.6:1 with the ratio of chloritic mole.
6. according to the goods of claim 1, wherein water content is below 5 % by weight.
7. according to the goods of claim 1, described organic hydrocarbon is the straight chain organic hydrocarbon that comprises 16 or 18 carbon.
8. according to the goods of claim 1, wherein organic hydrocarbon is selected from hexadecanol, octadecanol, 16 octadecanols, hexadecane, octadecane, stearic acid, stearate and combination thereof.
9. goods according to Claim 8, wherein said stearate is selected from: magnesium stearate, sodium stearate.
10. according to the goods of claim 1, its in water when suspendible aqueous solution be shown as alkalescence.
The method of the goods of 11. preparation claim 1 to 10 any one, it comprises the following steps:
(a) aqueous solution that preparation comprises chlorite and alkaline matter;
(b) aqueous suspensions that preparation comprises organic hydrocarbon;
The aqueous solution that (b ') preparation comprises basic salt;
(c) to the solution and the suspension that add step (a), step (b) and step (b ') gained in porous carrier, mix homogeneously, so that chlorite, alkaline matter, organic hydrocarbon and the basic salt in porous carrier adsorbent solution and suspension;
(d) make step (c) gained mixture dry, make water content lower than 5%, pack, to obtain final product.
12. produce and/or discharge the method for chlorine dioxide in substantially controlled mode, and the method comprises the following steps:
(i) provide the goods of claim 1 to 10 any one, before using, these goods are wrapped in the container of the packaging material that can completely cut off moisture and circulation of air, so that these goods did not substantially produce and/or discharge chlorine dioxide before using;
(ii) in the time using these goods, described container is opened, to allow that the moisture outside container contacts with these goods with air, and produced and/or release chlorine dioxide.
13. according to the method for claim 12, wherein opens by control the amount that the mode control moisture of described vessel port size contacts with these goods with air, thereby controls the speed that chlorine dioxide produces and/or discharges.
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| WO2014138000A1 (en) * | 2013-03-05 | 2014-09-12 | University Of Florida Research Foundation, Inc. | Chlorine dioxided generator using redox resin and adsorbed chlorite salt |
| CN103341193B (en) * | 2013-07-25 | 2015-12-23 | 孙晓晖 | Overall process airtight adsorption type fumigation method |
| TWI754614B (en) * | 2015-06-03 | 2022-02-11 | 日商大幸藥品股份有限公司 | Method for deactivating airborne microorganisms in space |
| CN106082131A (en) * | 2016-06-02 | 2016-11-09 | 四川齐力绿源水处理科技有限公司 | Liquid chlorine dioxide releasing agent and preparation method |
| CN108651453A (en) * | 2018-04-28 | 2018-10-16 | 张志� | A kind of slow released ClO 2 disinfectant and preparation method thereof |
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| CN108782552A (en) * | 2018-08-09 | 2018-11-13 | 中昊(大连)化工研究设计院有限公司 | The new process for producing of chlorine dioxide slow-release piece |
| CN111943143A (en) * | 2019-05-17 | 2020-11-17 | 浙江金海环境技术股份有限公司 | Chlorine dioxide generating agent composition, preparation method and application |
| JP7464463B2 (en) | 2019-06-28 | 2024-04-09 | 日揮触媒化成株式会社 | Chlorine Compound Adsorbent |
| KR102423077B1 (en) * | 2020-04-10 | 2022-07-21 | 주식회사 알엔비즈 | Preparation method of chlorine dioxide gas carrier & discharge kit capable of high adsorption capacity and emission persistency |
| CN111972412A (en) * | 2020-08-27 | 2020-11-24 | 上海辉文生物技术股份有限公司 | Chlorine dioxide slow-release composition and production process thereof |
| CN112299375B (en) * | 2020-11-10 | 2022-06-14 | 深圳凯士洁生物技术有限公司 | Preparation method of solid slow-release chlorine dioxide |
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| CN101177244A (en) * | 2006-11-06 | 2008-05-14 | 叶青 | Preparation of solid chlorine dioxide |
| EP2130795A4 (en) * | 2007-03-15 | 2012-12-19 | Taiko Pharmaceutical Co Ltd | Composition for stabilizing chlorine dioxide |
| CN101785498A (en) * | 2010-03-12 | 2010-07-28 | 国家农产品保鲜工程技术研究中心（天津） | Freshness preservative pad used for edible fungi storage and use method thereof |
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