Method for producing recycled water-absorbent resin, and method for producing water-absorbent resin using recycled water-absorbent resin as part of raw material

Abstract

To provide a method for producing a recycled water-absorbent resin that can yield a recycled water-absorbent resin excelling in color tone as well as water-soluble content and durability.SOLUTION: A method for producing a recycled water-absorbent resin includes a cleaning step and / or a dehydration step for recovered water-absorbent resin, an addition step for adding a metal chelating agent to the recovered water-absorbent resin, and a drying step, where the addition step is performed after the cleaning step and / or dehydration step.SELECTED DRAWING: None

Description

[Technical field]

[0001] The present invention relates to a method for producing a recycled water-absorbent resin, and a method for producing a water-absorbent resin using a recycled water-absorbent resin as part of a raw material. [Background technology]

[0002] In recent years, absorbent resins have been widely used as water absorbents in absorbent articles such as paper diapers, sanitary napkins, and incontinence pads, as constituent materials thereof, from the viewpoint of absorbing body fluids. Examples of such absorbent resins include hydrolyzates of starch-acrylonitrile graft copolymers, neutralized products of starch-acrylic acid graft polymers, saponified products of vinyl acetate-acrylic acid ester copolymers, and crosslinked products of partially neutralized acrylic acid polymers. Among them, from the viewpoint of water absorption performance, polyacrylic acid (salt)-based absorbent resins using acrylic acid and / or its salt as a monomer are most widely produced industrially, and many technologies related to such absorbent resins have been disclosed.

[0003] Although absorbent articles are generally disposable, interest in recycling absorbent articles is increasing due to the rise in environmental awareness. Known techniques for recycling absorbent resins used in absorbent articles include a technique in which a superabsorbent polymer derived from used absorbent articles is inactivated, treated with ozone water, then reactivated with an alkaline aqueous solution, and then hydrophilic fine particles are added and dried (Patent Document 1), a technique in which an alkali metal ion source is added to a regeneration aqueous solution containing a superabsorbent polymer inactivated by acid, and the resulting wet superabsorbent recycled polymer is dried (Patent Document 2), a technique having a step of obtaining a superabsorbent polymer that has been primarily dehydrated by immersing a sanitary product component material containing a superabsorbent polymer in an acid-containing aqueous solution, and a step of contacting the primarily dehydrated superabsorbent polymer with a polyvalent metal ion source (Patent Document 3), and a technique in which used superabsorbent polymer is dehydrated, and then a particle group of the superabsorbent polymer is attached, and then dried to suppress adhesion and coloring of the particles to each other (Patent Document 4). [Prior art documents] [Patent documents]

[0004] [Patent Document 1] International Publication No. WO2020 / 241025 [Patent Document 2] International Publication No. WO2019 / 151538 [Patent Document 3] International Publication No. WO2023 / 007871 [Patent Document 4] International Publication No. WO2021 / 205780 Summary of the Invention [Problem to be solved by the invention]

[0005] However, the recycled water-absorbent resin obtained by the above-mentioned conventional techniques has room for improvement in terms of color tone, water-soluble content, and durability.

[0006] In the above-mentioned circumstances, one aspect of the present invention is to provide a method for producing a recycled water-absorbing resin, which can provide a recycled water-absorbing resin excellent in color tone, water-soluble content and durability. [Means for solving the problem]

[0007] In order to solve the above problems, one embodiment of the present invention includes the following configuration.

[0008] [1] A method for producing a recycled water absorbent resin from a water absorbent resin recovered from used absorbent articles and / or waste generated in the process of producing a water absorbent resin, comprising a washing step for washing the water absorbent resin and / or a dehydration step for dehydrating the water absorbent resin, an addition step (A) for adding a metal chelating agent (A) (excluding a monovalent carboxylic acid (salt) consisting only of CHO and a polyvalent carboxylic acid (salt) consisting only of CHO) to the water absorbent resin, and a drying step for drying the water absorbent resin, wherein the addition step (A) is performed after the washing step and / or the dehydration step.

[0009] [2] The method for producing a recycled water-absorbing resin according to [1], wherein the water-absorbing resin is a water-absorbing resin recovered from one or more types of used absorbent articles and / or one or more types of waste generated in the manufacturing process of the water-absorbing resin.

[0010] [3] The method for producing a recycled water absorbent resin according to [1] or [2], wherein the water absorbent resin recovered from the used absorbent article and / or waste generated in the production process of the water absorbent resin contains a metal chelating agent (B).

[0011] [4] The method for producing a recycled water absorbent resin according to any one of [1] to [3], wherein the metal chelating agent (A) is (i) a polyvalent phosphoric acid (salt) having a plurality of nitrogen atoms, and / or (ii) a polyvalent carboxylic acid (salt) other than a polyvalent carboxylic acid (salt) consisting only of CHO, and is a polyvalent carboxylic acid (salt) having a plurality of nitrogen atoms.

[0012] [5] The method for producing a recycled water absorbent resin according to any one of [1] to [4], further comprising an addition step (B) of adding an inorganic reducing agent to the water absorbent resin after the washing step and / or the dehydration step.

[0013] [6] The method for producing a recycled water absorbent resin according to any one of [1] to [5], wherein the water absorbent resin recovered from the used absorbent article and / or waste generated in the process of producing the water absorbent resin contains one or more polyvalent metal cations selected from the group consisting of calcium ions, magnesium ions, and aluminum ions.

[0014] [7] The method for producing the recycled water absorbent resin according to [6], wherein the amount of the metal chelating agent (A) used is 2 times or more and 1000 times or less by mass relative to the total mass of the polyvalent metal cations in the recycled water absorbent resin.

[0015] [8] The method for producing a recycled water absorbent resin according to any one of [1] to [7], wherein the amount of the metal chelating agent (A) used is 0.01 mass% or more and 2.00 mass% or less with respect to 100 mass% of the recycled water absorbent resin. Effect of the Invention

[0016] According to one aspect of the present invention, there can be provided a method for producing a recycled water-absorbing resin, which can provide a recycled water-absorbing resin having excellent color tone, water-soluble content and durability. Furthermore, there can be provided a method for producing a water-absorbing resin using the recycled water-absorbing resin as a part of a raw material for the water-absorbing resin. DETAILED DESCRIPTION OF THE PREFERRED EMBODIMENTS

[0017] <1. Manufacturing method of recycled water absorbent resin> [1-1] Technical Concept of the First Embodiment of the Present Invention The present inventors have found that recycled water absorbent resins obtained by recycling water absorbent resins contained in used absorbent articles and waste materials generated during the manufacturing process of water absorbent resins have poor color tone (large YI value and yellowing). The yellowing of water absorbent resins may give consumers an unpleasant impression. Therefore, there is a problem that water absorbent resins with poor color tone (large YI value and yellowing) are unsuitable for product applications due to their hygienic feel.

[0018] In order to improve the color tone of the recycled water absorbent resin, the present inventors have investigated the use of a bleaching agent in the recycling process of the water absorbent resin. As a result, the present inventors have found that when a bleaching agent is used in an amount sufficient to sufficiently improve the color tone (i.e., sufficient bleaching effect is exhibited), the resulting recycled water absorbent resin is inferior in water soluble matter and durability. The present inventors have speculated that this is because the bleaching agent can also function as a decomposition agent for the water absorbent resin. Furthermore, the present inventors have speculated that the yellowing of the recycled water absorbent resin is due to the presence of residual substances derived from body fluids such as human waste, or residual monomers in the manufacturing process of the water absorbent resin. Based on this speculation, the present inventors have further studied the above problem. As a result, the present inventors have surprisingly found that by adding a metal chelating agent to a used water absorbent resin and / or a water absorbent resin derived from waste in a recycling process of the water absorbent resin, in other words, by carrying out a step of adding a metal chelating agent in the recycling process, a recycled water absorbent resin excellent in color tone, water soluble matter and durability can be provided, and have completed the present invention. Such a recycled water absorbent resin excellent in color tone, water soluble matter and durability is a recycled water absorbent resin with low environmental load, but is comparable to a normal (unused) water absorbent resin, and can be suitably used for product applications (for example, sanitary material applications).

[0019] [1-2] Method for producing recycled water absorbent resin according to the first embodiment of the present invention In a first embodiment of the present invention, there is provided a method for producing a recycled water absorbent resin from a water absorbent resin (recovered water absorbent resin) recovered from used absorbent articles and / or waste generated in the manufacturing process of the water absorbent resin, the method comprising a washing step for washing the water absorbent resin and / or a dehydration step for dehydrating the water absorbent resin, an addition step (A) for adding a metal chelating agent (A) (excluding a monovalent carboxylic acid (salt) consisting only of CHO and a polyvalent carboxylic acid (salt) consisting only of CHO) to the water absorbent resin, and a drying step for drying the water absorbent resin, the addition step (A) being performed after the washing step and / or the dehydration step. Hereinafter, the "production method of a recycled water absorbent resin according to the first embodiment of the present invention" may be referred to as "this first production method". "Consisting only of CHO" means "consisting only of carbon element, hydrogen element and oxygen element".

[0020] According to the first manufacturing method of the present invention, it is possible to provide a recycled water absorbent resin that is excellent in color tone, water extractable content, and durability. According to the first manufacturing method of the present invention, it is also possible to provide a recycled water absorbent resin that is excellent in water absorption performance (for example, water absorption speed). According to the first manufacturing method of the present invention, it is also possible to provide a recycled water absorbent resin that has little or no odor. The "color tone" ("YI value" and "color"), "water extractable content", "durability", "water absorption speed", and "odor" of the water absorbent resin (recycled water absorbent resin) can be measured or evaluated by the methods described in the Examples.

[0021] [1-2-1] Absorbent articles In this specification, the term "absorbent article" refers to an article used for absorbing water. An example of the "absorbent article" is an absorbent article having an absorbent body containing a water-absorbing resin and a fibrous material, a top sheet having liquid permeability, and a back sheet having liquid impermeability. The absorbent body is preferably manufactured by blending the water-absorbing resin with the fibrous material, or by sandwiching the water-absorbing resin between the fibrous material and molding it into a shape such as a film, a tube, or a sheet. Here, the fibrous material may be hydrophilic fiber, such as pulverized wood pulp, cotton linters, crosslinked cellulose fiber, rayon, cotton, wool, acetate, vinylon, etc. Specific examples of the "absorbent article" include sanitary materials (sanitary products) such as paper diapers, sanitary napkins, adult incontinence products (incontinence pads), and pet sheets, but are not limited thereto.

[0022] The term "used absorbent article" in this first manufacturing method refers to an absorbent article (particularly, a sanitary material) that has absorbed any liquid (absorbed liquid), particularly bodily fluids such as urine and blood.

[0023] [1-2-2] Water-absorbing resin In this specification, the term "water-absorbent resin" refers to a water-swellable, water-insoluble polymer gelling agent, and generally refers to a conventional water-absorbent resin having a water absorption capacity of 10 to 1000 times its volume. More specifically, it is preferable that the water-absorbent resin before absorbing the liquid to be absorbed satisfies the physical property of CRC of 5 g / g or more as "water-swellable" specified in ERT441.2-02, and satisfies the physical property of Ext (water-soluble content) of 0 to 50 mass% as "water-insoluble" specified in ERT470.2-02.

[0024] Specific examples of water-absorbent resins include polyacrylic acid (salt)-based resins, polysulfonic acid (salt)-based resins, maleic anhydride (salt)-based resins, polyacrylamide-based resins, polyvinyl alcohol-based resins, polyethylene oxide-based resins, polyaspartic acid (salt)-based resins, polyglutamic acid (salt)-based resins, polyalginic acid (salt)-based resins, starch-based resins, and cellulose-based resins.

[0025] [1-2-3] Waste generated during the manufacturing process of water-absorbent resin In this specification, the term "waste generated during the manufacturing process of a water-absorbent resin" refers to a water-absorbent resin that is generated during the manufacturing process of a water-absorbent resin and is rejected from product use for some reason (for example, because its water-absorbing properties, color tone, etc. are not within the standard), and is usually discarded, and is therefore referred to as "waste." Examples of "waste generated during the manufacturing process of a water-absorbent resin" include, but are not limited to, fine powder, gel, and water-absorbent resin particles with excessively large or small particle diameters generated during the manufacturing process of a water-absorbent resin.

[0026] [1-2-4] Recycled water-absorbent resin In the present specification, the term "recycled water absorbent resin" refers to a water absorbent resin obtained by recycling a water absorbent resin containing a liquid to be absorbed, such as human waste, recovered from a used absorbent article and / or a water absorbent resin recovered from waste generated in the manufacturing process of the water absorbent resin, for an application requiring a water absorption function. In the present specification, such a water absorbent resin recovered from a used absorbent article and / or from waste generated in the manufacturing process of the water absorbent resin, in other words, a water absorbent resin to be recycled, may be referred to as a "recovered water absorbent resin". In addition, the recovered water absorbent resin may include a water absorbent resin contained in a water absorbent article discarded before use.

[0027] Usually, the recovered water absorbent resin does not have water absorption performance or has very low water absorption performance, and may contain a large amount of impurities derived from body fluids or generated during the manufacturing process of the water absorbent resin. Therefore, the recovered water absorbent resin is not used for product applications for water absorption such as absorbent articles, but is disposed of, thermally recycled as fuel, composted, or otherwise disposed of. On the other hand, the "recycled water absorbent resin" is a water absorbent resin derived from the recovered water absorbent resin, but is obtained by recovering the water absorption performance of the recovered water absorbent resin so that it can be used again for water absorption purposes. In other words, the "recycled water absorbent resin" is intended to be a water absorbent resin made from the recovered water absorbent resin as a raw material, has water absorption performance, and can be used for product applications such as absorbent articles.

[0028] [1-2-5] Cleaning process The first manufacturing method preferably includes a washing step of washing the recovered water absorbent resin. The washing step included in the first manufacturing method can be said to be a step of removing impurities (e.g., body fluids such as human waste, impurities generated during the manufacturing process, etc.) present between particles of the swollen gel of the recovered water absorbent resin, on the particle surfaces, etc., by washing with a washing liquid (washing treatment). Specific washing methods for the recovered water absorbent resin include, for example, a method of adding a washing liquid to the recovered water absorbent resin, a method of immersing the recovered water absorbent resin in a washing liquid, a method of stirring the recovered water absorbent resin while immersing it in a washing liquid, etc., but are not limited thereto.

[0029] The washing liquid used in the washing step is not particularly limited as long as it is an aqueous liquid that can wash away impurities and does not alter the recovered water absorbent resin, but it is preferable that the recovered water absorbent resin can absorb the washing liquid and swell because it can remove more impurities, especially impurities inside the recovered water absorbent resin. Examples of such washing liquids include deionized water, tap water, distilled water, physiological saline, seawater, etc. Among the above washing liquids, deionized water, tap water, or distilled water is preferable because of its excellent washing effect.

[0030] The temperature of the cleaning liquid in the cleaning step is not particularly limited, and can be from room temperature to 100° C., or steam of the cleaning liquid can be used. When using a high-temperature cleaning liquid or steam of the cleaning liquid of 60° C. or higher, it is preferable because a sterilizing effect can be expected in addition to the cleaning effect.

[0031] The amount of the washing liquid used in the washing step (total amount used) is not particularly limited as long as the recovered water absorbent resin can be sufficiently washed, but for example, it is preferably 2000 parts by mass or more, more preferably 10000 parts by mass or more, and even more preferably 100000 parts by mass or more, relative to 100 parts by mass of the recovered water absorbent resin.

[0032] When the first production method includes a washing step, the washing step needs to be carried out at least once, but may be carried out multiple times.

[0033] [1-2-6] Dehydration process The first manufacturing method preferably includes a dehydration step of dehydrating the recovered water absorbent resin, preferably the recovered water absorbent resin after the washing step. The dehydration step can also be said to be a step of dehydrating (dehydrating) the recovered water absorbent resin (preferably the swollen gel of the recovered water absorbent resin) to discharge impurities present inside the water absorbent resin together with moisture to the outside of the system.

[0034] In the dehydration step, the method of dehydrating the recovered water absorbent resin is not particularly limited, and is not particularly limited as long as it is a method capable of reducing the moisture content of the swollen recovered water absorbent resin in a state of absorbing liquid (for example, the aqueous liquid used for washing). Specific dehydration methods include, for example, a method of contacting the swollen gel of the recovered water absorbent resin with various dehydrating liquids such as an aqueous solution containing a hydrophilic organic solvent, an aqueous solution with a low pH (for example, 3 or less), and an aqueous solution of a polyvalent metal salt (for example, calcium chloride), as well as a method of applying a voltage to the swollen gel using a pair of electrodes. Methods of contacting the swollen gel of the recovered water absorbent resin with the various dehydrating liquids include, but are not limited to, a method of adding the liquid to the recovered water absorbent resin gel (swollen gel) in a swollen state, a method of immersing the swollen gel in the liquid, and a method of stirring the swollen gel while immersing it in the liquid.

[0035] In the dehydration step, when the swollen gel of the recovered water absorbent resin is immersed in an aqueous solution containing a hydrophilic organic solvent, the concentration of the hydrophilic organic solvent in the aqueous solution in which the recovered water absorbent resin is immersed is preferably 35% by mass or more, more preferably 40% by mass or more, and even more preferably 45% by mass or more.

[0036] In this specification, the hydrophilic organic solvent refers to an organic solvent having a solubility of 20 g or more in 100 mL of water at 20° C. As the hydrophilic organic solvent, one having a solubility of 25 g or more in 100 mL of water at 20° C. is more preferable, and one having a solubility of 30 g or more in 100 mL of water at 20° C. is even more preferable.

[0037] Specific examples of such hydrophilic organic solvents include: (1) lower alcohols such as methanol, ethanol, n-propyl alcohol, isopropyl alcohol, tert-butyl alcohol, etc.; (2) ketones such as acetone, methyl ethyl ketone, etc.; (3) ethers such as tetrahydrofuran, dioxane, etc.; and (4) esters such as methyl acetate, methyl lactate, ethyl lactate, etc. These hydrophilic organic solvents may be used alone or in combination of two or more.

[0038] In the dehydration step, when the swollen gel of the water-absorbent resin is immersed in an aqueous solution with a low pH (for example, 3 or less), the pH of the aqueous solution is preferably 3 or less, and more preferably 0.5 to 2.5. As the aqueous solution, an aqueous solution containing an acid can be suitably used. As such an acid, either an inorganic acid or an organic acid can be used. In the case of an inorganic acid, for example, hydrochloric acid, sulfuric acid, etc. can be used. In the case of an organic acid, for example, tartaric acid, glycolic acid, malic acid, citric acid, succinic acid, acetic acid, etc. can be used. These acids may be used alone or in combination of two or more.

[0039] In the dehydration step, when the swollen gel of the recovered water absorbent resin is contacted with an aqueous solution of a polyvalent metal salt, examples of the polyvalent metal salt include salts of metals such as calcium, magnesium, aluminum, iron, cobalt, nickel, and copper with chlorine, carbonate, acetate, etc. These polyvalent metal salts may be used alone or in combination of two or more.

[0040] When the first production method includes a dehydration step, the dehydration step may be performed at least once, but may be performed multiple times. When the first production method includes a washing step in addition to the dehydration step, the dehydration step is preferably performed after the washing step.

[0041] The first production method may include at least one of the above-mentioned washing step and dehydration step, or may include both the washing step and the dehydration step.

[0042] [1-2-7] Drying process The first manufacturing method includes a drying step of drying the recovered water absorbent resin. The drying step is a step of drying the recovered water absorbent resin in a moist state until the resin solid content is a desired value. The resin solid content of the water absorbent resin is determined from the loss on drying of the water absorbent resin (the change in mass before and after heating 1 g of the water absorbent resin at 180° C. for 3 hours), and is preferably 80% by mass or more, more preferably 85% by mass to 99% by mass, even more preferably 90% by mass to 98% by mass, and particularly preferably 92% by mass to 97% by mass.

[0043] In the drying step, the method for drying the recovered water absorbent resin is not particularly limited, but examples thereof include heat drying, hot air drying, reduced pressure drying, fluidized bed drying, infrared drying, microwave drying, drum dryer drying, drying by azeotropic dehydration with a hydrophobic organic solvent, and superheated steam drying using high-temperature steam. Among these, from the viewpoint of drying efficiency, hot air drying is preferred as the drying method, and band drying in which hot air drying is performed on a ventilation belt is more preferred. In addition, in the drying step, only one of these drying methods may be performed, or two or more may be combined and performed.

[0044] When hot air drying is performed in the drying step, the drying temperature (hot air temperature) in the hot air drying is preferably 120°C or more and 250°C or less, more preferably 150°C or more and 200°C or less, from the viewpoint of the color tone and drying efficiency of the obtained recycled water absorbent resin. The drying conditions other than the above drying temperature, such as the wind speed of the hot air and the drying time, can be appropriately set according to the moisture content, total mass and target resin solid content of the recovered water absorbent resin to be dried. In addition, when band drying is performed, known drying conditions, for example, conditions described in International Publication Nos. 2006 / 100300, 2011 / 025012, 2011 / 025013, and 2011 / 111657, can be appropriately applied as drying conditions.

[0045] [1-2-8] Addition step (A) In this specification, the metal chelating agent used in the addition step (A) is referred to as the metal chelating agent (A) for the sake of convenience. In this specification, the metal chelating agent (A) and the metal chelating agent (B) described below may be collectively referred to simply as the "metal chelating agent". In this specification, when an embodiment related to a metal chelating agent is described without the use of symbols such as (A) and (B), such an embodiment is intended to apply to both the metal chelating agent (A) and the metal chelating agent (B).

[0046] By adding the metal chelating agent (A) to the recovered water absorbent resin, when the recovered water absorbent resin contains polyvalent metals derived from human waste, the polyvalent metals can be captured, and the presence of the polyvalent metals in the form of ions in the water absorbent resin can be reduced or prevented. As a result, the recycled water absorbent resin obtained has an advantage of being excellent in color tone without using a bleaching agent. In addition, by carrying out the addition step (A), the recycled water absorbent resin obtained has an advantage of being excellent in water soluble matter and durability. In addition, by carrying out the addition step (A), the recycled water absorbent resin obtained has an advantage of being excellent in water absorption performance (e.g., water absorption speed) without carrying out excessive purification.

[0047] In actual collection of used absorbent articles, used sanitary materials of various types and manufacturers can be collected without distinction between types and manufacturers. In addition, various manufacturers manufacture various types of water-absorbent resins, and the water-absorbent resins can be collected from waste generated in the manufacturing process of each of these manufacturers without distinction between types and manufacturers. Therefore, the recovered water-absorbent resins may include used water-absorbent resins of various manufacturers and various types. In other words, in this first manufacturing method, the water-absorbent resin (recovered water-absorbent resin) may be a water-absorbent resin recovered from one or more types of used absorbent articles and / or one or more types of waste generated in the manufacturing process of one or more types of water-absorbent resins.

[0048] Conventionally, when a recycled water absorbent resin is obtained from recovered water absorbent resins containing various manufacturers and various types of water absorbent resins, the water absorption performance of the obtained recycled water absorbent resin may not be stable. However, since the manufacturing method of the recycled resin according to one embodiment of the present invention has the addition step (A), even when recycled water absorbent resins derived from various manufacturers and various types of water absorbent resins are recycled, it has the advantage of being able to provide a recycled water absorbent resin that is excellent in color tone, excellent in water soluble matter and durability, excellent in water absorption speed, and has little or no odor.

[0049] As used herein, the term "metal chelating agent" refers to a compound that has multiple reactive functional groups in one molecule that can bind to a metal contained in a polyvalent metal salt, thereby having the ability to form a complex with the metal.

[0050] Examples of reactive functional groups include carboxyl groups and phosphate groups. In a preferred embodiment, the metal chelating agent preferably has 2 or more carboxyl groups or phosphate groups in one molecule, more preferably has 3 or more, for example, 3 or more to 100 or less, more preferably has 3 or more to 20 or less, and even more preferably has 3 or more to 10 or less. In a preferred embodiment, the metal chelating agent preferably has 2 or more carboxyl groups and phosphate groups in one molecule in total, more preferably has 3 or more, for example, 3 or more to 100 or less, more preferably has 3 or more to 20 or less, and even more preferably has 3 or more to 10 or less.

[0051] Examples of metal chelating agents include monovalent carboxylic acids (salts), polyvalent carboxylic acids (salts), monovalent amino carboxylic acids (salts), amino polyvalent carboxylic acids (salts), polyphosphoric acids (salts), and organic phosphonic acids (salts). Among these, amino polyvalent carboxylic acids (salts) and polyphosphoric acids (salts) are preferred. These may be used alone or in combination of two or more.

[0052] Examples of polyvalent carboxylic acids (salts) include citric acid, tartaric acid, malic acid, succinic acid, oxalic acid, and their D-, L- and meso-isomers, as well as salts thereof.

[0053] However, with regard to the metal chelating agent (A), the scope of the metal chelating agent (A) excludes monovalent carboxylic acids (salts) consisting of only CHO and polyvalent carboxylic acids (salts) consisting of only CHO.

[0054] Examples of the amino polycarboxylic acid (salt) include iminodiacetic acid, hydroxyethyliminodiacetic acid, nitrilotriacetic acid, nitrilotripropionic acid, ethylenediaminetetraacetic acid, hydroxyethylenediaminetriacetic acid, hexamethylenediaminetetraacetic acid, diethylenetriaminepentaacetic acid, triethylenetetraminehexaacetic acid, trans-1,2-diaminocyclohexanetetraacetic acid, bis(2-hydroxyethyl)glycine, diaminopropanoltetraacetic acid, ethylenediamine-2-propionic acid, glycol ether diaminetetraacetic acid, bis(2-hydroxybenzyl)ethylenediaminediacetic acid, ethylenediaminedisuccinic acid, L-glutamic acid diacetic acid, 3-hydroxy-2,2'-iminodisuccinic acid, glycol ether diaminetetraacetic acid, methylglycine diacetic acid, and salts thereof.

[0055] Examples of polyphosphoric acids (salts) include pyrophosphoric acid, tripolyphosphoric acid, tetrapolyphosphoric acid, metaphosphoric acid, and salts thereof.

[0056] Examples of organic phosphonic acids (salts) include 1-hydroxyethylidene-1,1-diphosphonic acid, aminotrimethylenephosphonic acid, ethylenediaminetetra(methylenephosphonic acid), diethylenetriaminepenta(methylenephosphonic acid), etc. Examples of organic phosphonic acids (salts) that are particularly preferably used include 1-hydroxyethylidene-1,1-diphosphonic acid, ethylenediaminetetra(methylenephosphonic acid), and diethylenetriaminepenta(methylenephosphonic acid).

[0057] Specific examples of metal chelating agents include hydroxy polycarboxylic acids, amino polycarboxylic acids, organic polyphosphates, inorganic polyphosphates, amino polyphosphates, and tropolone derivatives. At least one compound selected from the group consisting of these compounds is applied in one embodiment of the present invention. The term "polyvalent" refers to having multiple functional groups in one molecule. The above-mentioned polyvalent compounds (hydroxy polycarboxylic acids, amino polycarboxylic acids, organic polyphosphates, inorganic polyphosphates, amino polyphosphates, etc.) preferably have 2 to 30 functional groups in one molecule, more preferably 3 to 20 functional groups in one molecule, and even more preferably 4 to 10 functional groups in one molecule.

[0058] From the viewpoint of the influence on polymerization and the physical properties of the obtained water absorbent resin, the molecular weight of the metal chelating agent is preferably 100 to 5000, more preferably 200 to 1000. When the molecular weight is 5000 or less, there is no risk of the aqueous monomer solution becoming thickened regardless of the timing of adding the metal chelating agent. That is, the molecular weight is preferably 5000 or less, since polymerization control and uniform mixing are facilitated.

[0059] Specific examples of the hydroxy polyvalent carboxylic acid include malic acid, citric acid, and salts thereof.

[0060] Specific examples of the amino polycarboxylic acid include iminodiacetic acid, hydroxyethyliminodiacetic acid, nitrilotriacetic acid, nitrilotripropionic acid, ethylenediaminetetraacetic acid, diethylenetriaminepentaacetic acid, triethylenetetraminehexaacetic acid, trans-1,2-diaminocyclohexanetetraacetic acid, N,N-bis(2-hydroxyethyl)glycine, diaminopropanoltetraacetic acid, ethylenediamine2propionic acid, N-hydroxyethylethylenediaminetriacetic acid, glycol ether diaminetetraacetic acid, diaminopropanetetraacetic acid, N,N'-bis(2-hydroxybenzyl)ethylenediamine-N,N'-diacetic acid, 1,6-hexamethylenediamine-N,N,N',N'-tetraacetic acid, and salts thereof.

[0061] Specific examples of the organic polyphosphate include nitriloacetic acid-di(methylenephosphinic acid), nitrilodiacetic acid-(methylenephosphinic acid), nitriloacetic acid-β-propionic acid-methylenephosphonic acid, nitrilotris(methylenephosphonic acid), 1-hydroxyethylidene diphosphonic acid, and salts thereof.

[0062] Specific examples of the inorganic polyphosphate include pyrophosphoric acid, tripolyphosphoric acid, and salts thereof.

[0063] Specific examples of the amino polyphosphate include ethylenediamine-N,N'-di(methylenephosphinic acid), ethylenediaminetetra(methylenephosphinic acid), cyclohexanediaminetetra(methylenephosphonic acid), ethylenediamine-N,N'-diacetic acid-N,N'-di(methylenephosphonic acid), ethylenediamine-N,N'-di(methylenephosphonic acid), ethylenediaminetetra(methylenephosphonic acid), polymethylenediaminetetra(methylenephosphonic acid), diethylenetriaminepenta(methylenephosphonic acid), and salts thereof.

[0064] Specific examples of the tropolone derivatives include tropolone, β-thujaplicin, and γ-thujaplicin.

[0065] The metal chelating agent preferably contains a polyvalent phosphoric acid (salt) and / or a polyvalent carboxylic acid (salt) having a plurality of nitrogen atoms. More specifically, the metal chelating agent preferably contains one or more selected from the group consisting of amino polyvalent carboxylic acids, organic polyvalent phosphoric acids, amino polyvalent phosphoric acids, and salts thereof, among the above-mentioned metal chelating agents, and more preferably contains only one or more selected from the group. The metal chelating agent more preferably contains one or more selected from the group consisting of amino polyvalent carboxylic acids having three or more carboxyl groups in one molecule and salts thereof, and more preferably contains only one or more selected from the group. Furthermore, from the viewpoint of gel stability, the metal chelating agent more preferably contains one or more selected from the group consisting of diethylenetriaminepentaacetic acid, triethylenetetraminehexaacetic acid, trans-1,2-diaminocyclohexanetetraacetic acid, and salts thereof, and even more preferably contains only one or more selected from the group.

[0066] When the metal chelating agent is a salt, a monovalent salt, particularly an alkali metal salt such as a sodium salt or a potassium salt, an ammonium salt, or an amine salt can be preferably used, with the sodium salt and potassium salt being particularly preferred.

[0067] Examples of methods for adding the metal chelating agent (A) to the recovered water absorbent resin include, but are not limited to, adding the metal chelating agent (A) as is, adding the metal chelating agent (A) in a solution or slurry state, and the like.

[0068] In the first production method, the timing of performing the addition step (A), i.e., the timing of adding the metal chelating agent (A), is not particularly limited as long as it is after the washing step (if the washing step is performed multiple times, the last washing step) and / or after the dehydration step (if the dehydration step is performed multiple times, the last dehydration step). The addition step (A) can be performed, for example, after the washing step and before the dehydration step, after the washing step and during the dehydration step, before the grinding step described below, during the grinding step, after the grinding step, before the drying step, during the drying step, after the drying step, before the addition step (B) described below, during the addition step (B), after the addition step (B), before the surface cross-linking step described below, during the surface cross-linking step, or after the surface cross-linking step. Since there is an advantage that the deterioration of the recycled water absorbent resin can be suppressed, the addition step (A) is preferably performed before the drying step (for example, between the washing step and / or the dehydration step and the drying step), and more preferably during the grinding step. That is, in the first manufacturing method, the addition step (A) is preferably performed between the washing step and / or the dehydration step and the drying step, and more preferably during the pulverization step. An example of a method for performing the addition step (A) during the pulverization step is to feed the metal chelating agent (A) together with the recovered water absorbent resin to a pulverizer, and mix the recovered water absorbent resin and the metal chelating agent (A) in the pulverizer while pulverizing the recovered water absorbent resin. An example of a method for performing the addition step (A) during the addition step (B) is to add the metal chelating agent (A) and the inorganic reducing agent together to the recovered water absorbent resin. More specifically, the metal chelating agent (A), the inorganic reducing agent, and water (e.g., deionized water) may be mixed to prepare an aqueous solution, and then the obtained aqueous solution may be added to the recovered water absorbent resin.

[0069] In this first manufacturing method, the addition step (A) may be carried out at least once, but may be carried out multiple times. In this first manufacturing method, when the addition step (A) is carried out multiple times, it is preferable to carry out the addition step (A) after the washing step and / or dehydration step and before and after the drying step, for example, during the grinding step and after the surface crosslinking. That is, in this first manufacturing method, it is preferable to carry out the addition step (A) at least once after the washing step and / or dehydration step and before the drying step, and at least once after the drying step (at least twice in total).

[0070] The amount (addition amount) of the metal chelating agent (A) used in the addition step (A) is not particularly limited, but for example, it is preferably 0.001% by mass or more and 5.0% by mass or less with respect to 100% by mass of the finally obtained recycled water absorbent resin, and in the following order, it is preferably 0.02% by mass or more and 1.0% by mass or less, 0.03% by mass or more and 0.9% by mass or less, 0.04% by mass or more and 0.8% by mass or less, 0.05% by mass or more and 0.7% by mass or less, 0.06% by mass or more and 0.6% by mass or less, and most preferably 0.07% by mass or more and 0.5% by mass or less. When the amount of the metal chelating agent (A) used is 0.001% by mass or more and 5.0% by mass or less with respect to 100% by mass of the recycled water absorbent resin, the obtained recycled resin has excellent color tone, excellent water soluble content and durability, excellent water absorption speed, and has the advantage of having almost or no odor.

[0071] The recovered water absorbent resin may contain one or more polyvalent metal cations selected from the group consisting of polyvalent metal cations, for example, calcium ions, magnesium ions, and aluminum ions. The polyvalent metal cations in the recovered water absorbent resin are derived from, for example, polyvalent metal cations or polyvalent metal salts used in the manufacturing process of the water absorbent resin, or body fluids such as human waste. In addition, when an aqueous solution of a polyvalent metal salt is used in the dehydration step, a part of the polyvalent metal salt may be ionized to generate a polyvalent metal cation. In addition, when a polyvalent metal salt is used in the regeneration step described below, a part of the polyvalent metal salt may be ionized to generate a polyvalent metal cation. In addition, when a polyvalent metal salt is used as a surface cross-linking agent in the surface cross-linking step described below, a part of the polyvalent metal salt may be ionized to generate a polyvalent metal cation. Therefore, the finally obtained recycled water absorbent resin may also contain one or more polyvalent metal cations selected from the group consisting of calcium ions, magnesium ions, and aluminum ions. One of the purposes of adding the metal chelating agent (A) is to capture polyvalent metal cations in the recycled water absorbent resin. Therefore, the amount of metal chelating agent used (addition amount) in the addition step (A) is preferably set appropriately according to the total mass of polyvalent metal cations in the finally obtained recycled water absorbent resin. The total mass of polyvalent metal cations in the finally obtained recycled water absorbent resin depends on the amount of polyvalent metal cations contained in the recovered water absorbent resin, the amount of polyvalent metal cations derived from the polyvalent metal salt used in the manufacturing process of the recycled water absorbent resin, etc. The amount of metal chelating agent (A) used (addition amount) in the addition step (A) is preferably, for example, 2 times or more and 1000 times or less of the total mass of polyvalent metal cations in the recycled water absorbent resin. The amount of polyvalent metal cations in the recycled water absorbent resin can be measured by a method such as ICP emission spectroscopy.

[0072] The amount of the metal chelating agent in the finally obtained recycled water absorbent resin is preferably 0.01% by mass or more and 2.00% by mass or less, more preferably 0.05% by mass or more and 1.50% by mass or less, and even more preferably 0.10% by mass or more and 1.0% by mass or less, based on 100% by mass of the recycled water absorbent resin. The amount of the metal chelating agent in the finally obtained recycled water absorbent resin is preferably 2 times or more and 1000 times or less, more preferably 2.5 times or more and 500 times or less, and even more preferably 3 times or more and 100 times or less, relative to the total mass of the polyvalent metal cations in the recycled water absorbent resin. The amount of the metal chelating agent in the finally obtained recycled water absorbent resin depends on the amount of the metal chelating agent (A) added in the addition step (A) and the amount of the metal chelating agent (B) contained in the recovered water absorbent resin. The metal chelating agent may be consumed by decomposition or the like under high temperature conditions. Therefore, for example, when the addition step (A) is performed before the drying step, a part of the metal chelating agent (A) may be consumed by decomposition or the like as the recovered water absorbent resin dries in the drying step. That is, the total amount of the metal chelating agent (A) used in the addition step (A) may not be included in the finally obtained recycled water absorbent resin. Therefore, it is preferable to set the amount of the metal chelating agent (A) used in the addition step (A) so that the amount of the metal chelating agent in the finally obtained recycled water absorbent resin falls within the above-mentioned range, taking into consideration the timing of performing the addition step (A), the processing contents of the recovered water absorbent resin containing the metal chelating agent (A), and the amount of the metal chelating agent (B) contained in the recovered water absorbent resin.

[0073] [1-2-9] Metal chelating agents (B) The recovered water absorbent resin may contain a metal chelating agent (metal chelating agent (B)) for reasons such as the use of a metal chelating agent in the manufacturing process of the water absorbent resin before use of the recovered water absorbent resin. In this specification, the metal chelating agent contained in the recovered water absorbent resin is also referred to as the metal chelating agent (B) for convenience. In other words, in this first manufacturing method, the water absorbent resin recovered from used absorbent articles and / or the water absorbent resin recovered from waste generated in the manufacturing process of the water absorbent resin may contain the metal chelating agent (B).

[0074] The metal chelating agent (B) also includes monocarboxylic acids (salts) consisting of only CHO and polycarboxylic acids (salts) consisting of only CHO (for example, citric acid, tartaric acid, malic acid, succinic acid, oxalic acid, and their D-, L- and meso-isomers, as well as their salts, etc.).

[0075] [1-2-10] Addition step (B) It is preferable that the first production method further comprises an adding step (B) of adding an inorganic reducing agent to the recovered water absorbent resin.

[0076] The inorganic reducing agent is not particularly limited, but for example, a sulfur-based inorganic reducing agent is preferable, and examples thereof include sodium sulfite, potassium sulfite, calcium sulfite, ammonium sulfite, sulfurous acid, sodium hydrogen sulfite, potassium hydrogen sulfite, ammonium hydrogen sulfite, sodium thiosulfate, potassium thiosulfate, ammonium thiosulfate, and magnesium thiosulfate. One or more of these may be used. Among these, sulfites and hydrogen sulfites are preferable in terms of effect and cost.

[0077] Examples of the method for adding the inorganic reducing agent to the recovered water absorbent resin include, but are not limited to, a method in which the inorganic reducing agent is added as is, a method in which the inorganic reducing agent is added in the form of a solution or a slurry, and the like.

[0078] The amount of inorganic reducing agent used (addition amount) in the addition step (B) is not particularly limited, but is preferably 0.05 parts by mass or more and 10 parts by mass or less, and more preferably 0.1 parts by mass or more and 8 parts by mass or less, relative to 100 parts by mass of the water absorbent resin. When the amount of inorganic reducing agent used in the addition step (B) is 0.05 parts by mass or more relative to 100 parts by mass of the water absorbent resin, it has the advantage that the residual monomer reduction effect can be sufficiently obtained. When the amount of inorganic reducing agent used in the addition step (C) is 10 parts by mass or less relative to 100 parts by mass of the water absorbent resin, it is an appropriate amount to be added for the required residual monomer reduction effect, there is no risk of deterioration of physical properties, and it is also advantageous in terms of cost.

[0079] [1-2-11] Crushing process The first manufacturing method preferably includes a pulverization step in which the recovered water absorbent resin, preferably the recovered water absorbent resin after the washing step, more preferably the recovered water absorbent resin after the washing step and the dehydration step, is pulverized by a screw extruder such as a kneader or a meat chopper, or a pulverizer such as a cutter mill. The pulverization step is preferably performed before the drying step, and specifically, is preferably performed between the washing step and the dehydration step, and the drying step. When the first manufacturing method includes a pulverization step, it has an advantage that the drying efficiency is improved.

[0080] Regarding the grinding conditions and forms other than those described above, the contents disclosed in WO 2011 / 126079 are preferably applied to the present invention.

[0081] [1-2-12] Sterilization / disinfection process The first production method may include a sterilization / disinfection step of sterilizing and / or disinfecting the recovered water absorbent resin, preferably the recovered water absorbent resin after the washing step.

[0082] As a method for sterilizing and / or disinfecting the water absorbent resin, for example, a method of treating the water absorbent resin with a disinfectant solution can be mentioned. The disinfectant solution is not particularly limited, and a known one can be used. For example, sodium hypochlorite aqueous solution, chlorine dioxide aqueous solution, ozone water, hydrogen peroxide water, electrolytic water (acidic electrolytic water), etc. can be mentioned. The sterilization and disinfection are preferably carried out in a tank having an agitator blade, or by convection of the aqueous solution, etc., to efficiently mix the recovered water absorbent resin with the disinfectant solution.

[0083] In the present first manufacturing method, the timing of carrying out the sterilization / disinfection step is not particularly limited. The sterilization / disinfection step can be carried out before the drying step, for example, in parallel with (1) the washing step and / or the crushing (cutting) step described below, or after (2) the washing step and / or the crushing (cutting) step described below. That is, in the present first manufacturing method, it is preferable to carry out the sterilization / disinfection step between the washing step and / or the crushing (cutting) step and the drying step.

[0084] [1-2-13] Regeneration process The recovered water absorbent resin used in the first production method may have no water absorption performance or may have very low water absorption performance (particularly when the recovered water absorbent resin is a recovered water absorbent resin derived from used absorbent articles), but by subjecting the recovered water absorbent resin to a regeneration step, it is possible to impart (regenerate) sufficient water absorption performance (sufficient for product applications) to the recovered water absorbent resin.

[0085] The regeneration method of the recovered water absorbent resin in the regeneration step is not particularly limited as long as it restores the water absorption ability of the recovered water absorbent resin. For example, a method of contacting a polyvalent metal salt with a recovered water absorbent resin that has absorbed urine, dehydrating the resin, treating the resin with an acidic solution, neutralizing the resin with an alkali metal salt, and then drying the resin (JP Patent Publication No. 2003-225645); a method of contacting a recovered water absorbent resin that has absorbed urine with a solution containing a hydrophilic organic solvent, dehydrating the resin, and then drying the resin (JP Patent Publication No. 2003-326161); a method of contacting a polyvalent metal salt with a recovered water absorbent resin that has absorbed urine, dehydrating the resin, treating the resin with an aqueous alkali metal salt solution, subjecting the resin to ion exchange treatment, and then drying the resin (JP Patent Publication No. 2013-198862); a method of contacting a recovered water absorbent resin that has absorbed urine with an acidic aqueous solution, dehydrating the resin, neutralizing the resin with an alkali metal salt, and then drying the resin (JP Patent Publication No. 2019-135046, etc.); and other known regeneration methods can be used.

[0086] In the first production method, the timing of carrying out the regeneration step is not particularly limited. For example, the regeneration step is preferably carried out after the washing step and / or the dehydration step.

[0087] [1-2-14] Crushing (cutting) process The first manufacturing method may include a crushing (cutting) step of crushing (cutting) used absorbent articles into crushed (cut) materials.

[0088] In the crushing (cutting) step, the method of crushing (cutting) the used absorbent article is not particularly limited, and may be a method of cutting using a cutting tool such as a cutter. By carrying out the crushing (cutting) step, it is possible to increase the contact opportunity between the recovered water-absorbent resin in the absorbent article and the cleaning water, etc., thereby improving the cleaning effect and the speed thereof. It is also possible to facilitate separation of each component such as the water-absorbent resin, pulp, nonwoven fabric, etc. from the used absorbent article in the separation step described below.

[0089] In the first manufacturing method, the timing of performing the crushing (cutting) step is not particularly limited. The crushing (cutting) step is preferably performed after the washing step and / or the dehydration step, for example, but the crushing (cutting) step and the washing step may be performed simultaneously, the crushing (cutting) step and the dehydration step may be performed simultaneously, or the crushing (cutting) step, the washing step and the dehydration step may all be performed simultaneously.

[0090] [1-2-15] Separation process The first manufacturing method may include a separation step of separating the water-absorbent resin from a used absorbent article. "Separating the water-absorbent resin from a used absorbent article" refers to taking out the water-absorbent resin that has shrunk by discharging the absorbed liquid from gaps in the pulp, nonwoven fabric, etc. contained in the used absorbent article, and dispersing it in a treatment liquid.

[0091] As a method for separating the water-absorbing resin from the used absorbent article, for example, a method of stirring a mixture of the treatment liquid and the used absorbent article can be mentioned. The water-absorbing resin dispersed in the treatment liquid can be recovered by a conventional solid-liquid separation means for separating soluble and insoluble substances, for example, filtration, centrifugation, etc.

[0092] In the first manufacturing method, the timing of carrying out the separation step is not particularly limited. For example, the separation step is preferably carried out after the washing step and / or the dehydration step. For example, the separation step is more preferably carried out between the washing step and / or the dehydration step and the above-mentioned addition step. In addition, the above-mentioned crushing (cutting) step and the separation step can be carried out in parallel (simultaneously).

[0093] [1-2-16] Other processes In addition to the above-mentioned steps, the first production method may include any steps (other steps) that can be carried out in the production process of a normal water absorbent resin, such as a classification step of classifying the obtained recycled water absorbent resin, a surface cross-linking step of surface cross-linking the obtained recycled water absorbent resin, etc. As specific aspects of the other steps in the first production method, for example, the aspects described in the classification step section, the surface cross-linking step section, etc. of the second embodiment described later can be appropriately adopted.

[0094] [1-2-17] Color tone (yellowness index / YI value) of recycled water absorbent resin obtained by the first manufacturing method The YI value of the recycled water absorbent resin obtained by the first manufacturing method is preferably less than 20.0, more preferably 19.0 or less, more preferably 18.0 or less, even more preferably 17.0 or less, and particularly preferably 16.0 or less. The lower limit of the YI value of the recycled water absorbent resin is not particularly limited and may be 0. The YI value of the water absorbent resin is an index indicating the color tone of the water absorbent resin, and the YI value of the recycled water absorbent resin within the above range means that the coloring of the recycled water absorbent resin is more suppressed. The YI value of the water absorbent resin (recycled water absorbent resin) can be measured by the method described in the Examples.

[0095] [1-2-18] Water absorption properties of recycled water absorbent resin obtained by the first manufacturing method The water absorption properties of the recycled water absorbent resin obtained by the first manufacturing method are preferably 25.0 g / g or more in CRC, more preferably 30.0 g / g or more, even more preferably 35.0 g / g or more, and particularly preferably 36.0 g / g or more. Also, the AAP (0.3 psi) is preferably 12.0 g / g or more, more preferably 15.0 g / g or more, more preferably 18.0 g / g or more, more preferably 20.0 g / g or more, more preferably 22.0 g / g or more, more preferably 24.0 g / g or more, more preferably 26.0 g / g or more, more preferably 28.0 g / g or more, and particularly preferably 29.0 g / g or more. The water absorption rate (Vortex) is preferably less than 70 seconds, more preferably 69 seconds or less, more preferably 65 seconds or less, more preferably 60 seconds or less, more preferably 58 seconds or less, more preferably 55 seconds or less, even more preferably 53 seconds or less, and particularly preferably 50 seconds or less. The CRC, AAP (0.3 psi) and / or water absorption rate (Vortex) of the water absorbent resin (recycled water absorbent resin) being in the above range means that the water absorbent resin (recycled water absorbent resin) has excellent water absorption properties. The CRC, AAP (0.3 psi) and water absorption rate (Vortex) of the water absorbent resin (recycled water absorbent resin) can be measured by the method described in the Examples.

[0096] [1-2-19] Water-soluble fraction of recycled water-absorbent resin obtained by the first manufacturing method The water-soluble content of the recycled water absorbent resin obtained by the first manufacturing method is preferably less than 30% by mass, more preferably 25% by mass or less, and more preferably 20% by mass or less. The lower limit of the water-soluble content of the recycled water absorbent resin is not particularly limited, but is at least greater than 0% by mass. The water-soluble content of the recycled water absorbent resin can be measured by the method described in the Examples.

[0097] [1-2-20] "EDANA" and "ERT" "EDANA" is an abbreviation for European Disposables and Nonwovens Associations. Also, "ERT" is an abbreviation for EDANA Recommended Test Methods. In one embodiment of the present invention, unless otherwise specified, the physical properties of the water-absorbent resin are measured in accordance with the original ERT (revised in 2002 / publicly known document).

[0098] [1-2-21] Other In this specification, unless otherwise specified, "ppm" means "ppm by mass."

[0099] In this specification, "acid (salt)" means "acid and / or its salt." "(Meth)acrylic" means "acrylic and / or methacrylic."

[0100] In this specification, the unit of volume "liter" may be written as "l" or "L".

[0101] <2. Manufacturing method of water-absorbent resin containing recycled water-absorbent resin as part of the raw material> [2-1] Technical Concept of the Second Embodiment In actual recycling sites for used absorbent articles, sanitary materials of various types and manufacturers are recycled together. Therefore, with conventional technology, the water absorbent resins recovered therefrom are also mixed with those from various manufacturers and with various performances, making it difficult to obtain a recycled water absorbent resin with stable water absorption performance. As described above, with the first manufacturing method, a recycled water absorbent resin having excellent water absorption properties, at least water-soluble content and durability, can be provided, and a recycled water absorbent resin having excellent water absorption speed can be provided.

[0102] On the other hand, in order to meet various applications and required characteristics, the water absorbent resin for sanitary materials may be required to have a highly balanced water absorption property such as water soluble content, durability, and water absorption speed, as well as water absorption capacity, water absorption capacity under pressure, and liquid permeability. In other words, the water absorbent resin for sanitary materials may be required to have an excellent balance of various water absorption properties. However, as described above, recycled water absorbent resins often have unstable water absorption properties, and it is preferable to adjust the balance of various water absorption properties in order to use recycled water absorbent resins for sanitary materials.

[0103] Therefore, the inventors thought that by mixing the recycled water absorbent resin, which has unstable water absorption properties as described above, into part of the raw materials used when newly producing a water absorbent resin, it would be easy to adjust the balance of various water absorption properties such as water soluble content, durability, and water absorption speed, as well as water absorption capacity, water absorption capacity under pressure, and liquid permeability. Note that "newly producing a water absorbent resin" refers to the production of a conventional (normal) water absorbent resin using monomers constituting the water absorbent resin as raw materials. In this case, the conventional (normal) water absorbent resin does not include resins that partially contain the above-mentioned recycled water absorbent resin, nor water absorbent resins that use monomers generated by recycling as part of the raw materials.

[0104] Then, it was found that by using the recycled water absorbent resin produced by the above-mentioned first production method as a recycled water absorbent resin which is a part of the raw material, a water absorbent resin containing the recycled water absorbent resin as a part of the raw material, which is excellent in color tone, water extractable content and durability, and further has an excellent balance of other water absorption properties, can be obtained, and the second embodiment of the present invention was completed.

[0105] [2-2] Method for producing water-absorbent resin according to the second embodiment of the present invention In a second embodiment of the present invention, a method for producing a water-absorbent resin is provided, in which a recycled water-absorbent resin obtained by the first production method is used as a part of a raw material in a production process of the water-absorbent resin using a monomer constituting the water-absorbent resin as a raw material. Hereinafter, the "production method for an absorbent resin according to the second embodiment of the present invention" may be referred to as the "second production method".

[0106] According to the second production method, it is possible to provide a water absorbent resin that contains a recycled water absorbent resin as a part of a raw material, and that has excellent color tone, water-soluble content and durability, and is also excellent in balance of water absorption properties.

[0107] In the present second production method, "production of a water absorbent resin using a monomer constituting a water absorbent resin as a raw material" refers to a production method of a normal (non-recycled) water absorbent resin using a monomer constituting a water absorbent resin as a raw material, for example, a production method of a normal (non-recycled) water absorbent resin including a step of preparing an aqueous monomer solution, a polymerization step, a gel crushing step, a gel drying step, a classification step, and a surface cross-linking step. Therefore, one embodiment of the present second production method can also be expressed as a production method for a water absorbent resin including a step of preparing a monomer aqueous solution, a polymerization step, a gel crushing step, a gel drying step, a classification step and a surface cross-linking step, the production method including a washing step of washing the recovered water absorbent resin and / or a dehydration step of dehydrating the recovered water absorbent resin, an addition step (A) of adding a metal chelating agent (A) (excluding a monovalent carboxylic acid (salt) consisting only of CHO and a polyvalent carboxylic acid (salt) consisting only of CHO) to the recovered water absorbent resin, and a drying step of drying the recovered water absorbent resin, the addition step (A) being performed after the washing step and / or the dehydration step, and using a recycled water absorbent resin obtained by a recycling method for a recovered water absorbent resin (i.e., a recycled water absorbent resin obtained by the present first production method) as a part of a raw material.

[0108] A specific embodiment of the second production method will be described in detail below, taking as an example a method including a step of preparing an aqueous monomer solution, a polymerization step, a gel crushing step, a gel drying step, a classification step, and a surface cross-linking step.

[0109] In addition, with regard to the definitions and specific aspects of the "absorbent article", "water-absorbent resin", and "recycled water-absorbent resin" according to the second embodiment of the present invention, as well as the first manufacturing method ("cleaning process", "dehydration process", "addition process (A)", "drying process", "pulverization process", "sterilization / disinfection process", "regeneration process", "crushing (cutting) process" and "separation process"), the descriptions in the above-mentioned first embodiment are appropriately cited.

[0110] [2-2-1] Preparation of monomer aqueous solution The second production method preferably includes a monomer aqueous solution preparation step of preparing an aqueous solution containing acrylic acid (salt) as a main component (hereinafter referred to as "monomer aqueous solution"). In the second production method, a monomer slurry liquid can be used in addition to the monomer aqueous solution within a range in which the water absorption performance of the obtained water absorbent resin is not deteriorated, but for the sake of convenience, the monomer aqueous solution will be described in this section.

[0111] The above-mentioned "main component" means that the amount (content) of acrylic acid (salt) used is 50 mol% or more in the total amount (100 mol%) of monomers (in other words, monomers contained in the aqueous monomer solution, excluding the internal crosslinking agent) to be subjected to the polymerization reaction of the water absorbent resin. The content of acrylic acid (salt) in the total amount (100 mol%) of monomers is preferably 70 mol% or more, and more preferably 90 mol% or more (upper limit: 100 mol%).

[0112] (acrylic acid) As a monomer serving as a raw material for the water absorbent resin in the second production method, acrylic acid and / or a salt thereof (hereinafter referred to as "acrylic acid (salt)") is used from the viewpoints of the physical properties and productivity of the resulting water absorbent resin.

[0113] The term "acrylate" refers to acrylic acid neutralized with a basic composition. The acrylate may be a commercially available acrylate (e.g., sodium acrylate) or may be one obtained by neutralization in a water absorbent resin manufacturing plant.

[0114] (Basic Composition) In the present specification, the term "basic composition" refers to a composition containing a basic compound. More specifically, the basic compound may be an alkali metal carbonate and / or hydrogen carbonate, an alkali metal hydroxide, ammonia, an organic amine, or the like. Among these, from the viewpoint of the physical properties of the obtained water absorbent resin, a strongly basic basic compound, for example, an alkali metal hydroxide such as sodium hydroxide, potassium hydroxide, or lithium hydroxide, is preferred, and sodium hydroxide is more preferred.

[0115] (neutralization) In the second production method, it is preferable to neutralize at least a part of the acrylic acid. As the neutralization in the second production method, either neutralization of the acrylic acid (before polymerization) or neutralization of the hydrogel polymer obtained by polymerizing the acrylic acid (after polymerization) (hereinafter referred to as "post-neutralization") can be selected or used in combination. In addition, the mode of these neutralizations is not particularly limited, and may be a continuous type or a batch type, but a continuous type is preferable from the viewpoint of production efficiency, etc.

[0116] Regarding the conditions such as the neutralization device, neutralization temperature, and residence time, the conditions described in International Publication No. 2009 / 123197 and U.S. Patent Application Publication No. 2008 / 0194863 may be applied to one embodiment of the present invention.

[0117] The neutralization rate of the monomer (monomer having an acid group including acrylic acid) in the second production method is preferably 10 mol% to 90 mol%, more preferably 40 mol% to 85 mol%, further preferably 50 mol% to 80 mol%, and particularly preferably 60 mol% to 75 mol% in the total amount of the acid groups of the monomer (100 mol%). By setting the neutralization rate to 10 mol% or more, a water absorbent resin having a sufficient water absorption capacity can be provided, and by setting the neutralization rate to 90 mol% or less, a water absorbent resin having a higher water absorption capacity under pressure can be provided. The neutralization rate of the aqueous monomer solution will be further explained by taking as an example a case where the aqueous monomer solution contains only acrylic acid as a monomer component. In this case, the neutralization rate of the monomer is 75 mol% means that the monomer component contained in the aqueous monomer solution is a mixture of 25 mol% acrylic acid and 75 mol% acrylic acid salt. Such a mixture may be called a partially neutralized product of acrylic acid.

[0118] The above neutralization rate is the same in the case of post-neutralization. The above neutralization rate is also applied to the neutralization rate of the water-absorbent resin as a final product. In the second manufacturing method, the recycled water-absorbent resin is used as a part of the raw material in the manufacture of the water-absorbent resin. When such a recycled water-absorbent resin is used as a part of the raw material in the manufacture of the water-absorbent resin, the recycled water-absorbent resin may contain a basic compound. And, this basic compound may neutralize the acrylic acid before polymerization or the hydrogel-like crosslinked polymer after polymerization. Therefore, taking into account the neutralization by the basic compound derived from this recycled water-absorbent resin, the neutralization (post-neutralization) rate of the monomer in the aqueous monomer solution, the hydrogel-like polymer, and the water-absorbent resin as a final product is adjusted to a predetermined range.

[0119] (Other monomers) The aqueous monomer solution may contain a monomer (other monomer) other than the acrylic acid (salt). In the second production method, such other monomer can be used in combination with the acrylic acid (salt) to produce a water-absorbing resin.

[0120] The other monomer may be a water-soluble or hydrophobic unsaturated monomer. Specifically, anionic unsaturated monomers such as (anhydrous) maleic acid, fumaric acid, crotonic acid, itaconic acid, cinnamic acid, vinyl sulfonic acid, allyl toluene sulfonic acid, vinyl toluene sulfonic acid, styrene sulfonic acid, 2-(meth)acrylamido-2-methylpropanesulfonic acid, 2-(meth)acryloylethanesulfonic acid, 2-(meth)acryloylpropanesulfonic acid, and 2-hydroxyethyl (meth)acryloyl phosphate and / or salts thereof may be suitably used as the other monomer. Moreover, these other monomers may be used alone or in combination of two or more.

[0121] (Internal crosslinking agent) The aqueous monomer solution preferably contains an internal crosslinking agent. As the internal crosslinking agent that can be contained in the aqueous monomer solution, for example, the compounds described in U.S. Patent No. 6,241,928 can be mentioned. Among these, one or more compounds can be used as the internal crosslinking agent in consideration of reactivity.

[0122] When the polymerization step is carried out using an aqueous monomer solution containing an internal crosslinking agent, the resulting polymer may be internally crosslinked, and therefore the resulting polymer may be referred to as a "crosslinked polymer" or a "hydrous gel-like crosslinked polymer."

[0123] In addition, from the viewpoint of the water absorption performance of the obtained water absorbent resin, the internal crosslinking agent is preferably a compound having two or more polymerizable unsaturated groups, more preferably a compound having thermal decomposition properties at the drying temperature described below, and further preferably a compound having two or more polymerizable unsaturated groups having a (poly)alkylene glycol structural unit.

[0124] The polymerizable unsaturated group is preferably, for example, an allyl group or a (meth)acrylate group, more preferably a (meth)acrylate group. The (poly)alkylene glycol structural unit is preferably polyethylene glycol, and the number n is preferably 1 or more and 100 or less, more preferably 6 or more and 50 or less.

[0125] The amount of the internal crosslinking agent used (content in the aqueous monomer solution) is preferably 0.0001 mol% or more and 10 mol% or less, more preferably 0.001 mol% or more and 1 mol% or less, based on the total amount of the monomer. By setting the amount of the internal crosslinking agent used within the above range, a water-absorbing resin having a desired water-absorbing performance can be obtained. If the amount of the internal crosslinking agent used is less than 0.0001 mol%, the gel strength of the obtained water-absorbing resin tends to decrease and the water-soluble content tends to increase excessively, and if the amount of the internal crosslinking agent used is more than 10 mol%, the water absorption capacity of the obtained water-absorbing resin tends to decrease, which is not preferable. The mol% relative to the total monomer is the percentage of the number of moles of the internal crosslinking agent relative to the total number of moles of the monomer contained in the aqueous monomer solution.

[0126] In the second production method, a method is preferably applied in which a predetermined amount (within the above range) of an internal crosslinking agent is added to the monomer aqueous solution in advance, and the crosslinking reaction is started simultaneously with polymerization. On the other hand, in addition to this method, a method of post-crosslinking by adding an internal crosslinking agent during and / or after polymerization; a method of radical crosslinking using a radical polymerization initiator; a method of radiation crosslinking using active energy rays such as electron beams and ultraviolet rays, etc. can also be adopted. These methods can also be used in combination.

[0127] (Polymerization inhibitor) From the viewpoint of the polymerizability of acrylic acid and the color tone of the water-absorbing resin, the aqueous monomer solution preferably contains a polymerization inhibitor in an amount of 200 ppm or less, more preferably 10 ppm or more and 160 ppm or less, and even more preferably 20 ppm or more and 100 ppm or less. The polymerization inhibitor is not particularly limited, but is preferably a methoxyphenol, more preferably p-methoxyphenol.

[0128] The recovered water absorbent resin may contain a polymerization inhibitor (e.g., p-methoxyphenol) depending on the manufacturing process of the water absorbent resin from which it is derived. In that case, the recycled water absorbent resin obtained from the recovered water absorbent resin may also contain a polymerization inhibitor (e.g., p-methoxyphenol). In other words, the recycled water absorbent resin may contain p-methoxyphenol in the first manufacturing method. In addition, when a recycled water absorbent resin containing p-methoxyphenol is used as a part of the raw material, even if p-methoxyphenol is not used in the preparation step of the monomer aqueous solution, the water absorbent resin obtained by the second manufacturing method may contain p-methoxyphenol.

[0129] The aqueous monomer solution according to the second production method may contain impurities derived from each component in the aqueous monomer solution. For example, as for impurities derived from acrylic acid, the description of the compounds described in U.S. Patent Application Publication No. 2008 / 0161512 can be applied to the second embodiment of the present invention.

[0130] (Other substances) The aqueous monomer solution may contain substances (other substances) other than the above-mentioned components from the viewpoint of improving the physical properties of the resulting water-absorbing resin.

[0131] Examples of other substances include hydrophilic polymers such as starch, starch derivatives, cellulose, cellulose derivatives, polyvinyl alcohol, polyacrylic acid (salts), and crosslinked polyacrylic acid (salts); and other additives such as foaming agents such as carbonates and azo compounds, surfactants, chelating agents, and chain transfer agents.

[0132] When the aqueous monomer solution contains a hydrophilic polymer as an additional substance, the content of the hydrophilic polymer is preferably 50% by mass or less, more preferably 20% by mass or less, even more preferably 10% by mass or less, and particularly preferably 5% by mass or less (the lower limit is 0% by mass) relative to the total amount (100% by mass) of the aqueous monomer solution. When the aqueous monomer solution contains other additives as additional substances, the content of the other additives is preferably 5% by mass or less, more preferably 1% by mass or less, and even more preferably 0.5% by mass or less (the lower limit is 0% by mass) relative to the total amount (100% by mass) of the aqueous monomer solution.

[0133] The above-mentioned other substances may be added to the reaction system in the polymerization step described below. In this case, it is preferable that the total amount of the other substances contained in the aqueous monomer solution and the other substances added to the reaction system in the polymerization step is within the above-mentioned range.

[0134] When a water-soluble resin or a water-absorbent resin is used as the hydrophilic polymer, a graft polymer or a water-absorbent resin composition (e.g., a starch-acrylic acid polymer, a PVA-acrylic acid polymer, etc.) is obtained. These polymers and water-absorbent resin compositions also fall within the scope of one embodiment of the present invention.

[0135] [2-2-2] Polymerization process The second manufacturing method preferably includes a polymerization step of polymerizing the monomers (particularly, acrylic acid (salt)-based monomers) in the aqueous monomer solution obtained in the aqueous monomer solution preparation step to obtain a hydrous gel-like crosslinked polymer (hereinafter referred to as "hydrous gel").

[0136] (Polymerization initiator) In the polymerization step, it is preferable to carry out a polymerization reaction of the monomer using a polymerization initiator. The polymerization initiator used in the polymerization step is appropriately selected depending on the polymerization form and the like, and is not particularly limited. For example, a thermal decomposition type polymerization initiator, a photodecomposition type polymerization initiator, or a redox type polymerization initiator used in combination with a reducing agent that promotes the decomposition of these polymerization initiators can be mentioned. Specifically, one or more of the polymerization initiators disclosed in U.S. Pat. No. 7,265,190 can be suitably used. In addition, from the viewpoint of handling and the physical properties of the obtained water-absorbing resin, the polymerization initiator is preferably a peroxide or an azo compound, more preferably a peroxide, and even more preferably a persulfate.

[0137] The amount of the polymerization initiator used in the polymerization step is preferably 0.001 mol% or more and 1 mol% or less, more preferably 0.001 mol% or more and 0.5 mol% or less, based on the total amount of the monomers to be polymerized (monomers contained in the aqueous monomer solution). When a reducing agent is used in combination (i.e., when a redox polymerization initiator is used), the amount of the reducing agent used is preferably 0.0001 mol% or more and 0.02 mol% or less, based on the total amount of the monomers. The mol% relative to the monomer refers to the percentage of the number of moles of the polymerization initiator or reducing agent relative to the total number of moles of the monomers contained in the aqueous monomer solution.

[0138] In addition, instead of the above polymerization initiator, the polymerization reaction may be carried out by irradiation with active energy rays such as radiation, electron beams, and ultraviolet rays, or the polymerization reaction may be carried out by using these active energy rays in combination with the polymerization initiator.

[0139] (polymerization form) The polymerization form in the polymerization step is not particularly limited, but from the viewpoint of the water absorption properties of the obtained water absorbent resin and the ease of polymerization control, etc., preferably, spray droplet polymerization, aqueous solution polymerization, reversed phase suspension polymerization, more preferably aqueous solution polymerization, reversed phase suspension polymerization, and further preferably aqueous solution polymerization are mentioned. Among them, continuous aqueous solution polymerization is particularly preferable. Forms such as continuous belt polymerization and continuous kneader polymerization can also be applied. In addition, a foaming polymerization form in which bubbles (particularly inert gas, etc.) are dispersed in a monomer aqueous solution to carry out polymerization can also be applied.

[0140] As specific polymerization forms, continuous belt polymerization is disclosed in U.S. Patent Nos. 4,893,999, 6,241,928, U.S. Patent Application Publication No. 2005 / 215734, etc., and continuous kneader polymerization is disclosed in U.S. Patent Nos. 6,987,151, 6,710,141, etc. By adopting these continuous aqueous solution polymerizations, the production efficiency of the water absorbent resin can be improved.

[0141] The polymerization form may also be acid polymerization. Acid polymerization is a method of obtaining a polymer by polymerizing an acid group-containing monomer including unneutralized acrylic acid and then neutralizing it with a basic composition. A specific embodiment of acid polymerization is disclosed in JP-A-1-103606.

[0142] In addition, preferred forms of the continuous aqueous solution polymerization include "high-temperature initiated polymerization" and "high-concentration polymerization." "High-temperature initiated polymerization" refers to a form in which polymerization is initiated at a temperature of preferably 30°C or higher, more preferably 35°C or higher, even more preferably 40°C or higher, and particularly preferably 50°C or higher (upper limit is the boiling point). "High-concentration polymerization" refers to a form in which polymerization is performed at a monomer concentration of preferably 30% by mass or higher, more preferably 35% by mass or higher, even more preferably 40% by mass or higher, and particularly preferably 45% by mass or higher (upper limit is the saturated concentration). These polymerization forms can also be used in combination.

[0143] In the polymerization step, the polymerization can be carried out under a desired atmosphere, for example, under an air atmosphere, but from the viewpoint of the color tone of the obtained water absorbent resin, it is preferable to carry out the polymerization under an inert gas atmosphere such as nitrogen or argon. In this case, it is preferable to control the oxygen concentration to 1 volume % or less. It is also preferable to replace the dissolved oxygen in the aqueous monomer solution with an inert gas (for example, to make the dissolved oxygen less than 1 mg / l).

[0144] In one embodiment of the present invention, the polymerization may be carried out as foaming polymerization in which bubbles (particularly the above-mentioned inert gases or the like) are dispersed in an aqueous monomer solution.

[0145] [2-2-3] Gel crushing process The second manufacturing method preferably includes a gel crushing step in which the hydrogel obtained in the polymerization step is crushed by a screw extruder such as a kneader or a meat chopper, or a gel crusher such as a cutter mill, to obtain a particulate hydrogel (hereinafter referred to as a "particulate hydrogel"). When kneader polymerization is used as the polymerization form in the polymerization step, the polymerization step and the gel crushing step are carried out simultaneously. When a particulate hydrogel is directly obtained in the polymerization process, such as in gas phase polymerization or reversed phase suspension polymerization, the gel crushing step may not be carried out.

[0146] Regarding gel crushing conditions and forms other than those described above, the contents disclosed in WO 2011 / 126079 are preferably applied to the present invention.

[0147] [2-2-4] Gel drying process The second manufacturing method preferably includes a gel drying step in which the particulate hydrogel obtained in the polymerization step and / or gel crushing step is dried to a desired resin solid content to obtain a dried polymer. The resin solid content of the dried polymer is determined from the loss on drying (the change in mass when 1 g of the dried polymer is heated at 180° C. for 3 hours), and is preferably 80% by mass or more, more preferably 85% by mass to 99% by mass, even more preferably 90% by mass to 98% by mass, and particularly preferably 92% by mass to 97% by mass.

[0148] The method for drying the particulate hydrogel is not particularly limited, and examples thereof include heat drying, hot air drying, reduced pressure drying, fluidized bed drying, infrared drying, microwave drying, drum dryer drying, drying by azeotropic dehydration with a hydrophobic organic solvent, superheated steam drying using high-temperature steam, etc. Among these, from the viewpoint of drying efficiency, hot air drying is preferred, and band drying in which hot air drying is performed on a ventilation belt is more preferred.

[0149] The drying temperature (hot air temperature) in the hot air drying is preferably 120°C or higher and 250°C or lower, more preferably 150°C or higher and 200°C or lower, from the viewpoint of the color tone and drying efficiency of the obtained water-absorbent resin. The drying conditions other than the drying temperature, such as the hot air speed and drying time, can be appropriately set according to the water content and total mass of the particulate hydrogel to be dried and the intended resin solid content. In addition, when band drying is performed, the conditions described in International Publication Nos. 2006 / 100300, 2011 / 025012, 2011 / 025013, 2011 / 111657, etc. are appropriately applied as drying conditions.

[0150] [2-2-5] Classification process The second production method preferably includes a classification step of classifying the dried polymer obtained in the drying step to obtain a particulate dried polymer having a desired particle size.

[0151] In the classification step, the method for classifying the dried polymer includes sieve classification using a JIS standard sieve (JIS Z8801-1 (2000)), air flow classification, etc. Among them, from the viewpoint of classification efficiency, sieve classification is preferably selected.

[0152] The particle size of the particulate dry polymer obtained in the classification step is not particularly limited, but for example, the mass average particle size (D50) is preferably 200 μm to 500 μm, more preferably 250 μm to 450 μm, and even more preferably 300 μm to 400 μm. The proportion of particles smaller than 150 μm is preferably less than 5% by mass, more preferably 4% by mass or less, and even more preferably 3% by mass or less.

[0153] In the classification step, the dried polymer may be appropriately pulverized to obtain a particulate dried polymer of a desired particle size. The pulverization method is not particularly limited, and a high-speed rotary pulverizer such as a roll mill, a hammer mill, a screw mill, or a pin mill, a vibration mill, a knuckle type pulverizer, or a cylindrical mixer may be used.

[0154] [2-2-6] Surface crosslinking process The second production method preferably includes a surface cross-linking step, which is a step of providing a portion with a higher cross-linking density on the surface layer (a portion several tens of μm from the surface of the particulate dry polymer) of the particulate dry polymer obtained through the above-mentioned classification step. The surface cross-linking step is composed of a mixing step, a heat treatment step, and a cooling step (optional).

[0155] In the surface cross-linking step, a surface-cross-linked water-absorbent resin is obtained by radical cross-linking on the surface of the particulate dry polymer, surface polymerization, a cross-linking reaction with a surface cross-linking agent, etc. Therefore, the particulate dry polymer to be subjected to the surface cross-linking step can also be said to be a water-absorbent resin precursor.

[0156] (Surface cross-linking agent) In the surface crosslinking step, it is preferable to crosslink the surface of the particulate dried polymer using a surface crosslinking agent. The surface crosslinking agent is not particularly limited, but may be an organic or inorganic surface crosslinking agent. Among them, from the viewpoint of the physical properties of the water-absorbent resin, the handling property of the surface crosslinking agent, etc., an organic surface crosslinking agent that reacts with a carboxyl group is preferable. Specifically, as the surface crosslinking agent, one or more compounds disclosed in U.S. Patent No. 7,183,456 can be used. More specifically, as the surface crosslinking agent, polyhydric alcohol compounds, epoxy compounds, haloepoxy compounds, polyvalent amine compounds or condensates thereof with haloepoxy compounds, oxazoline compounds, oxazolidinone compounds, polyvalent metal salts, alkylene carbonate compounds, cyclic urea compounds, etc. may be used. One of these surface crosslinking agents may be used alone, or two or more may be used in combination. In addition, it is preferable to use these surface crosslinking agents in the state of an aqueous solution (i.e., in the state of a surface crosslinking liquid).

[0157] The amount of the surface crosslinking agent used in the surface crosslinking step (the total amount used when a plurality of agents are used) is preferably 0.01 to 10 parts by mass, more preferably 0.01 to 5 parts by mass, relative to 100 parts by mass of the particulate dry polymer. The surface crosslinking agent is preferably added in the form of an aqueous solution, and in this case, the amount of water used is preferably 0.1 to 20 parts by mass, more preferably 0.5 to 10 parts by mass, relative to 100 parts by mass of the particulate dry polymer. Furthermore, a hydrophilic organic solvent may be used in combination as necessary, and in that case, the amount of the hydrophilic organic solvent used is preferably 10 parts by mass or less, more preferably 5 parts by mass or less, relative to 100 parts by mass of the particulate dry polymer. Each additive added in the "re-wetting step" described later can also be mixed into the aqueous solution of the surface crosslinking agent within the range of 5 parts by mass or less.

[0158] (Mixing process) The surface crosslinking step includes a mixing step of mixing the particulate dry polymer with the above-mentioned surface crosslinking agent. The method of mixing the surface crosslinking agent in the mixing step is not particularly limited, but for example, a method of preparing a surface crosslinking agent solution in advance and mixing the solution with the particulate dry polymer by preferably spraying or dropping, more preferably spraying, can be mentioned.

[0159] The device for mixing the particulate dry polymer and the surface crosslinking agent is not particularly limited, but is preferably a high-speed stirring type mixer, more preferably a high-speed stirring type continuous mixer.

[0160] (Heat treatment process) The surface cross-linking step includes a heat treatment step in which the mixture discharged from the mixing step is heated to cause a cross-linking reaction on the surface of the particulate dry polymer. The heat treatment step can also be called a cross-linking reaction step.

[0161] The apparatus for carrying out the heat treatment is not particularly limited, but preferably includes a paddle dryer. The heating temperature in the heat treatment, in other words, the reaction temperature in the crosslinking reaction, is appropriately set according to the type of the surface crosslinking agent used, but is preferably 50°C or more and 300°C or less, more preferably 100°C or more and 200°C or less.

[0162] (cooling process) The surface cross-linking step preferably includes a cooling step of cooling the surface-cross-linked particulate dry polymer after the heat treatment.

[0163] In the cooling step, the cooling device is not particularly limited, but is preferably a device with the same specifications as the device used in the heat treatment step, and more preferably a paddle dryer. This is because it can be used as a cooling device by changing the heat medium to a refrigerant. In addition, the surface crosslinked particulate dry polymer obtained in the heat treatment step is forcibly cooled, if necessary, to preferably 40°C or more and 80°C or less, more preferably 50°C or more and 70°C or less, in the cooling step.

[0164] [2-2-7] Use of recycled water-absorbent resin In the second manufacturing method, the recycled water absorbent resin obtained in the first manufacturing method is used as a part of the raw material of the obtained water absorbent resin. In the second manufacturing method, "using the recycled water absorbent resin as a part of the raw material of the obtained water absorbent resin" means that the recycled water absorbent resin is added to the water absorbent resin raw material (for example, the monomer aqueous solution, the hydrogel, the dried polymer, and / or the particulate dried polymer) in any of the above-mentioned steps, specifically, in any of the steps of preparing the monomer aqueous solution, the polymerization step, the gel crushing step, the gel drying step, the classification step, and the surface crosslinking step.

[0165] The method of adding the recycled water absorbent resin to the water absorbent resin raw material is not particularly limited, and examples thereof include a method of adding the recycled water absorbent resin as it is, a method of adding the recycled water absorbent resin in a state of a swollen gel obtained by swelling the recycled water absorbent resin with water, a method of adding the recycled water absorbent resin in a state of being dispersed in water, a method of solubilizing the recycled water absorbent resin by a known method and adding it in a state of a solubilized polymer, and the like.

[0166] More specifically, when the recycled water absorbent resin is added in the "preparation step of the aqueous monomer solution", the recycled water absorbent resin may be added to the aqueous monomer solution, or the recycled water absorbent resin may be added to water in advance and then mixed with other raw materials such as monomers. From the viewpoint of uniform mixing of the raw materials, it is preferable to add the recycled water absorbent resin to the aqueous monomer solution.

[0167] When the recycled water absorbent resin is added in the "polymerization step", the recycled water absorbent resin may be added before the start of polymerization, or may be added after the start of polymerization. From the viewpoint of uniformity of the polymer component, it is preferable to add the recycled water absorbent resin before the start of polymerization.

[0168] When the recycled water absorbent resin is added in the "gel crushing step", the recycled water absorbent resin may be added before crushing, or may be added during crushing. It may also be added in portions. From the viewpoint of uniformity of the gel component, it is preferable to add the recycled water absorbent resin before gel crushing.

[0169] When the recycled water absorbent resin is added in the "gel drying step", the hydrous gel and the recycled water absorbent resin may be mixed before drying, or after drying. When the recycled water absorbent resin powder and the hydrous gel are mixed before drying, the moisture of the hydrous gel is transferred to the recycled water absorbent resin powder. Therefore, it is preferable because it is expected to have effects such as shortening the drying speed and reducing the generation of undried gel.

[0170] When the recycled water absorbent resin is added in the "classification step", the dried polymer and the recycled water absorbent resin may be mixed before or after classification. From the viewpoint of uniformity of particle size, it is preferable to add the recycled water absorbent resin before classification.

[0171] When the recycled water absorbent resin is added in the "surface cross-linking step", the particulate dried polymer and the recycled water absorbent resin may be mixed in advance, or may be treated without mixing. From the viewpoint of uniform mixing of the surface cross-linking liquid and the water absorbent resin, it is preferable to use the particulate recycled water absorbent resin and subject all the surface cross-linked materials (i.e., the particulate dried polymer and the particulate recycled water absorbent resin) to surface cross-linking in the form of particulates.

[0172] In the second manufacturing method, the recycled water absorbent resin may be added at any of the above timings. The entire amount of the recycled water absorbent resin may be added at one time at any timing, or may be added in portions at multiple timings. The recycled water absorbent resin may be added in different forms depending on the timing of addition.

[0173] In the second manufacturing method, the ratio of the recycled water absorbent resin to all the raw materials for the water absorbent resin is not particularly limited, but is preferably 1% by mass or more and 60% by mass or less, more preferably 1% by mass or more and 50% by mass or less, even more preferably 1% by mass or more and 40% by mass or less, and even more preferably 1% by mass or more and 30% by mass or less. In other words, in the second manufacturing method, it is preferable to add the recycled water absorbent resin so that the ratio of the recycled water absorbent resin to all the raw materials for the water absorbent resin is within the above range. The above-mentioned "all raw materials for the water absorbent resin" refers to all the raw materials used in the manufacturing process of the water absorbent resin (i.e., the total amount of the recycled water absorbent resin to be added and the water absorbent resin prepared from the aqueous monomer solution). More specifically, the raw materials include the recycled water absorbent resin, and the non-recycled water absorbent resin and its raw materials (e.g., acrylic acid (salt); basic composition; other monomers; internal crosslinking agents; other substances (starch, etc.); polymerization initiators; and surface crosslinking agents, etc.). The above ratio is the ratio of the solid content of the recycled water absorbent resin to the solid content of all the raw materials of the water absorbent resin.

[0174] [2-2-8] Color tone (yellowness index / YI value) of water-absorbent resin obtained by the second production method The YI value of the water-absorbent resin obtained by the second manufacturing method is preferably less than 20.0, more preferably 19.0 or less, more preferably 18.0 or less, even more preferably 17.0 or less, and particularly preferably 16.0 or less. The lower limit of the YI value of the water-absorbent resin is not particularly limited and may be 0. The YI value of the water-absorbent resin is an index showing the color tone of the water-absorbent resin, and the YI value of the water-absorbent resin within the above range means that the coloring of the water-absorbent resin is more suppressed. The YI value of the water-absorbent resin can be measured by the method described in the Examples.

[0175] [2-2-9] Water absorption properties of the water-absorbent resin obtained by the second manufacturing method The water absorption properties of the water absorbent resin obtained by the second manufacturing method are preferably 25.0 g / g or more, more preferably 30.0 g / g or more, even more preferably 35.0 g / g or more, and particularly preferably 36.0 g / g or more. Also, the AAP (0.3 psi) is preferably 12.0 g / g or more, more preferably 15.0 g / g or more, more preferably 18.0 g / g or more, more preferably 20.0 g / g or more, more preferably 22.0 g / g or more, more preferably 24.0 g / g or more, more preferably 26.0 g / g or more, more preferably 28.0 g / g or more, and particularly preferably 29.0 g / g or more. The water absorption rate (Vortex) is preferably less than 70 seconds, more preferably 69 seconds or less, more preferably 65 seconds or less, more preferably 60 seconds or less, more preferably 58 seconds or less, more preferably 55 seconds or less, even more preferably 53 seconds or less, and particularly preferably 50 seconds or less. The CRC, AAP (0.3 psi) and / or water absorption rate (Vortex) of the water absorbent resin in the above ranges means that the water absorbent resin has excellent water absorption properties. The CRC, AAP (0.3 psi) and water absorption rate (Vortex) of the water absorbent resin can be measured by the method described in the Examples.

[0176] [2-2-10] Water-soluble fraction of water-absorbent resin obtained by the second manufacturing method The water-soluble content of the water-absorbent resin obtained by the second manufacturing method is preferably less than 30% by mass, more preferably 25% by mass or less, and more preferably 20% by mass or less. The lower limit of the water-soluble content of the water-absorbent resin is not particularly limited, but is at least greater than 0% by mass. The water-soluble content of the water-absorbent resin can be measured by the method described in the Examples. EXAMPLES

[0177] The present invention will be described in more detail with reference to the following examples and comparative examples. However, the present invention is not limited to these examples. Examples obtained by appropriately combining the technical means disclosed in each example are also included in the scope of the present invention.

[0178] (Measurement and evaluation methods) The methods for measuring and evaluating each physical property in the examples and comparative examples are as follows.

[0179] (a) CRC The "CRC" of a water-absorbent resin is an abbreviation for "Centrifuge Retention Capacity" and indicates the absorption capacity (unit: g / g) of a water-absorbent resin for 30 minutes under no pressure with respect to a 0.90% by mass aqueous solution of sodium chloride. The specific method for measuring the CRC of a water-absorbent resin (recycled water-absorbent resin) was as follows.

[0180] 0.200 g of the water-absorbent resin was uniformly placed in a bag (85 mm x 60 mm) made of nonwoven fabric (manufactured by Nangoku Pulp Kogyo Co., Ltd., product name: Heatlon Paper, model: GSP-22) and heat-sealed. The bag (containing the water-absorbent resin) was immersed in a large excess (usually about 500 ml) of 0.90% by mass sodium chloride aqueous solution at room temperature. After 30 minutes, the bag was pulled out and drained for 3 minutes at a centrifugal force (250 G) described in ERT441.2-02 using a centrifuge (manufactured by Kokusan Co., Ltd., centrifuge: model H-122), and the mass W1 (g) of the bag was measured. In addition, the same operation was performed without using the water-absorbent resin, and the mass W0 (g) at that time was measured. From the measured values ​​of W1 and W0, the CRC of the control water-absorbent resin was calculated according to the following formula (1): CRC of absorbent resin (g / g) = (W1-W0) / (mass of absorbent resin)-1···Equation (1).

[0181] (b) AAP0.3 The "AAP" of a water-absorbent resin is an abbreviation for "Absorption Against Pressure" and indicates the absorbency (unit: g / g) against a 0.90% by mass aqueous sodium chloride solution. Also, "AAP0.3" means the AAP under a pressure of 0.3 psi.

[0182] The AAP0.3 of the above water-absorbent resin (recycled water-absorbent resin) was measured in accordance with ERT442.2-02. Specifically, 0.9 g of the water-absorbent resin was placed in a large excess of 0.9% by mass aqueous sodium chloride solution for 1 hour, and the AAP0.3 was measured at 2.07 kPa (21 g / cm 2 The value was measured after swelling under a pressure of 0.5 psi (0.3 psi).

[0183] (c) Color evaluation (yellowness index / YI value) The color tone evaluation (yellowness index / YI value) of the water-absorbent resin was performed using a spectrophotometer (Spectrophotometer SE7700) manufactured by Nippon Denshoku Industries Co., Ltd. Reflection measurement was selected as the measurement setting condition, and the measurement diameter was LAV (28 mm). The attached 35Φ×15H round cell, 35Φ×15H cell case, and standard white board for powder were used. About 1.5 g of the water-absorbent resin immediately after production was uniformly filled on the sample stage so that there was no gap on the bottom surface. Under the conditions of room temperature (20°C or higher and 25°C or lower) and humidity of 50 RH%, the YI value (yellowness index; Yellow Index, ASTM D1925) in the Hunter Lab color system of the water-absorbent resin immediately after production (recycled water-absorbent resin) was measured from the back side of the sample stage using the spectrophotometer.

[0184] (d) Color Tone Evaluation (Color Tone) The color tone (hue) of the water-absorbent resin was evaluated visually.

[0185] (e) Water soluble content According to ERT470.1-99, 1.0 g of the water-absorbent resin was stirred in 200 ml of physiological saline for 16 hours, and the water-soluble polymer content (mass%) in the filtrate was determined by pH titration, and the obtained value was taken as the water-soluble content.

[0186] (f) Water absorption rate (Vortex) 0.02 parts by mass of edible blue No. 1 (CAS number: 3844-45-9), a food additive, was added to 1.000 parts by mass of a 0.90% by mass aqueous sodium chloride solution (physiological saline) prepared in advance, and the liquid temperature was adjusted to 30°C. 50 ml of the physiological saline thus obtained was weighed into a 100 ml beaker with a body diameter of 55 mm and a height of 70 mm, and a cylindrical Teflon (registered trademark) magnetic stirrer with a length of 40 mm and a thickness of 8 mm was placed in the beaker. 2.0 g of water-absorbent resin was added while stirring the physiological saline at 600 rpm, and the water absorption rate (seconds) was measured. The start point of the water absorption rate measurement and the end point of the measurement were in accordance with the standards described in JIS K 7224 (1996) "Explanation of the water absorption rate test method for superabsorbent resins". Specifically, the water-absorbent resin was placed as uniformly as possible near the inner wall surface of the beaker, and then a timer was started (start point). The time (end point) until the saline solution was absorbed by the water-absorbent resin and the gelling saline solution covered the rotating stirrer tip (covered in a V shape when viewed from the cross section) was measured. The obtained time (seconds) was defined as the water absorption rate (seconds).

[0187] (g) Durability evaluation 20.0 g of physiological saline (at 37°C, simulating body temperature) containing 1.00 g of water-absorbent resin and 0.05% by mass of L-ascorbic acid was added to a sealed container with a capacity of 200 ml, and the container was sealed and allowed to swell 25 times. After 16 hours, the container was tilted 90° to check the state (fluidity) of the gel. If the gel had no fluidity, the durability was rated as "+ (excellent)", if the gel had fluidity, the durability was rated as "- (slightly poor)", and if the gel was in solution, the durability was rated as "-- (poor)". The standards for durability evaluation are shown in Table 1.

[0188] (h) Polyvalent metal cation content in water absorbent resin (recycled water absorbent resin) After adding nitric acid to the water absorbent resin, the obtained water absorbent resin was repeatedly heated and irradiated with microwaves in stages to obtain a decomposition product of the water absorbent resin. The polyvalent metal cation content in the water absorbent resin was quantified by performing ICP emission spectroscopy on the obtained decomposition product.

[0189] [Table 1]

[0190] In the durability evaluation, a fluidity of + (excellent) level or higher indicates that the recycled water absorbent resin being evaluated is a recycled water absorbent resin having excellent water absorption properties.

[0191] [Production Example 1] A reaction vessel was charged with 244.9 g of acrylic acid, 0.71 g (0.040 mol % relative to the carboxyl group-containing unsaturated monomer) of polyethylene glycol diacrylate (molecular weight 523) as an internal crosslinking agent, 103.7 g of 48.5 mass % aqueous sodium hydroxide solution, and 389.0 g of deionized water, and the mixture was mixed to prepare an aqueous monomer solution (S1').

[0192] Next, the monomer aqueous solution (S1') was cooled while stirring. When the liquid temperature reached 40.0°C, 100.9 g of a 48.5% by mass aqueous sodium hydroxide solution adjusted to 40°C was added and mixed to prepare a monomer aqueous solution (S1). At this time, the temperature of the monomer aqueous solution (S1) rose to 78.2°C due to the heat of neutralization in the second stage immediately after preparation. Immediately after starting to mix the 48.5% by mass aqueous sodium hydroxide solution, precipitates were observed, but they gradually dissolved and became a transparent homogeneous solution.

[0193] Next, 12.1 g of 4.0 mass% sodium persulfate aqueous solution was added to the stirred monomer aqueous solution (S1), and the mixture was immediately poured into a stainless steel bat-shaped container (bottom surface 340×340 mm, height 25 mm, inner surface; Teflon (registered trademark) coating) in an open-air system. The time from the start of the second stage neutralization to pouring the monomer aqueous solution (S1) into the bat-shaped container was 55 seconds, and a hot plate was used as the bat-shaped container, and the surface temperature was heated to 40° C. after the monomer aqueous solution (S1) was poured. The polymerization reaction started 60 seconds after the monomer aqueous solution (S1) was poured into the bat-shaped container. The polymerization reaction proceeded while the reactants expanded and foamed in all directions while generating water vapor. After the reaction, the reactants shrunk to a size slightly larger than the bat-shaped container. After 3 minutes had passed since the start of the polymerization reaction, the reactants were taken out as a hydrogel-like crosslinked polymer (hereinafter referred to as "hydrogel") (S1). This series of operations was carried out in an open atmosphere.

[0194] The hydrogel (S1) obtained by the polymerization reaction was cut into strips and crushed with a meat chopper having a die diameter of 7.5 mm. The crushed hydrogel (S1) was spread on a wire net with a mesh size of 50 mesh (opening size of 300 μm) and dried with hot air at 190° C. for 60 minutes to obtain a dried polymer (S1).

[0195] Next, the dried polymer (S1) was further pulverized using a vibration mill, and further classified using JIS standard sieves with mesh sizes of 850 μm and 150 μm, to obtain a water-absorbent resin precursor (S1) in an irregularly pulverized state.

[0196] A surface crosslinking agent solution consisting of 0.030 parts by mass of ethylene glycol diglycidyl ether, 1.35 parts by mass of propylene glycol, and 3.15 parts by mass of deionized water was uniformly mixed with 100 parts by mass of the obtained water absorbent resin precursor (S1), and the mixture was heat-treated at 100°C for 45 minutes, thereby performing surface crosslinking of the water absorbent resin precursor (S1).

[0197] The surface-crosslinked water-absorbent resin precursor (S1) was cooled and passed through a JIS standard sieve with a mesh size of 710 μm to obtain a water-absorbent resin (S1). The obtained water-absorbent resin (S1) had a CRC of 35.9 g / g, an AAP0.3 of 29.4 g / g, a YI value (yellowness index) of 10.3, and a water absorption speed (Vortex) of 50 seconds.

[0198] Next, 200 g of the obtained water absorbent resin (S1) and 6,000 g of artificial urine (a solution consisting of 1.9 mass% urea, 0.80 mass% sodium chloride, 0.10 mass% magnesium chloride hexahydrate, 0.10 mass% calcium chloride dihydrate, and 97.1 mass% ion-exchanged water) were added to a reaction kettle equipped with a stirrer, and the mixture was left at room temperature for 24 hours to obtain a simulated used water absorbent resin (1).

[0199] [Comparative Example 1] (Dehydration process) The entire amount of the simulated used water absorbent resin (1) obtained in Production Example 1 and 10,000 g of ethanol were added to a reaction vessel equipped with a stirrer, and the mixture was stirred for 15 minutes to carry out a dehydration treatment.

[0200] The simulated used water absorbent resin (C1) after the dehydration treatment was filtered through a 100 mesh (150 μm mesh size) stainless steel wire screen.

[0201] (Crushing process) Next, 800 g of the resulting filtrate after dehydration (corresponding to a solid content concentration of 24.4% by mass and a swelling ratio of approximately 3.1 times) was continuously fed into a meat chopper to crush the gel.

[0202] (drying process) The simulated used water absorbent resin (C1) after the gel crushing was dried in an oven at 190° C. for 2 hours.

[0203] (Classification process) Next, the dried simulated used water absorbent resin (C1) was pulverized using a vibration mill and further classified using JIS standard sieves with mesh sizes of 850 μm and 106 μm to obtain a recycled water absorbent resin precursor (C1) in an irregular crushed form.

[0204] (Surface crosslinking process) 100 parts by mass of the obtained recycled water absorbent resin precursor (C1) and a surface crosslinking agent solution consisting of 0.030 parts by mass of ethylene glycol diglycidyl ether, 1.35 parts by mass of propylene glycol, and 3.15 parts by mass of deionized water were uniformly mixed, and the mixture was heated at 100°C for 45 minutes to perform surface crosslinking of the recycled water absorbent resin precursor (C1).

[0205] The recycled water absorbent resin precursor (C1) after surface cross-linking was cooled, and then passed through a JIS standard sieve with a mesh size of 710 μm to obtain a recycled water absorbent resin (C1).

[0206] The obtained recycled water absorbent resin (C1) had a CRC of 36.3 g / g, an AAP0.3 of 29.7 g / g, a YI value (yellowness index) of 23.9, a water-soluble content of 16 mass % and a water absorption speed (Vortex) of 60 seconds.

[0207] [Comparative Example 2] In the grinding step in Comparative Example 1, 10.0 parts by mass of a 5.0% by mass aqueous hydrogen peroxide solution (0.50% by mass relative to 100% by mass of the absorbent resin) was continuously added to the meat chopper together with 800 g of the filtrate after dehydration treatment as a bleaching agent relative to 100 parts by mass of the solid content of the filtrate (i.e., 100 parts by mass of the absorbent resin) in the meat chopper, and the same operation as in Comparative Example 1 was performed to obtain a recycled absorbent resin (C2). The obtained recycled absorbent resin (C2) had a CRC of 36.1 g / g, an AAP0.3 of 29.3 g / g, a YI value (yellowness index) of 20.0, a water-soluble content of 17% by mass, and a water absorption speed (Vortex) of 63 seconds.

[0208] [Comparative Example 3] In the grinding step in Comparative Example 1, 10.0 parts by mass of a 30% by mass aqueous hydrogen peroxide solution (3.0% by mass relative to 100% by mass of the water absorbent resin) was continuously added to the meat chopper together with 800 g of the filtrate after dehydration treatment as a bleaching agent relative to 100 parts by mass of the solid content of the filtrate (i.e., 100 parts by mass of the water absorbent resin) in the meat chopper, and the same operation as in Comparative Example 1 was performed to obtain a recycled water absorbent resin (C3). The obtained recycled water absorbent resin (C3) had a CRC of 45.2 g / g, an AAP0.3 of 11.8 g / g, a YI value (yellowness index) of 11.3, a water-soluble content of 33% by mass, and a water absorption speed (Vortex) of 70 seconds.

[0209] [Example 1] In the pulverization step in Comparative Example 1, an aqueous solution of the metal chelating agent (A) consisting of 0.1 parts by mass of trisodium diethylenetriaminepentaacetate (A) and 4 parts by mass of deionized water was continuously added to the meat chopper together with 800 g of the filtrate after the dehydration treatment and 100 parts by mass of the solid content of the filtrate (i.e., 100 parts by mass of the water absorbent resin) (implementation of the addition step (A)). The same dehydration step, drying step, classification step and surface cross-linking step as in Comparative Example 1 were performed. By such operations, a surface-cross-linked recycled water absorbent resin (1A) containing 1000 ppm of the metal chelating agent (metal chelating agent (A)) was obtained.

[0210] Then, 100 parts by mass of the recycled water absorbent resin (1A) was uniformly mixed with an aqueous solution of the metal chelating agent (A) consisting of 0.01 part by mass of trisodium diethylenetriaminepentaacetate (A) and 1 part by mass of deionized water, and then dried at 60°C for 1 hour.

[0211] Thereafter, the obtained dried product was cooled, and the cooled product was passed through a JIS standard sieve with a mesh size of 710 μm to obtain a recycled water absorbent resin (1B). The obtained recycled water absorbent resin (1B) had a CRC of 36.1 g / g, an AAP0.3 of 29.3 g / g, a YI value (yellowness index) of 16.0, a water soluble content of 15 mass%, and a water absorption rate (Vortex) of 50 seconds. Table 2 shows the results of various measurements and evaluations of the recycled water absorbent resin (1B).

[0212] In Example 1, the amount of polyvalent metal cations in the finally obtained recycled water absorbent resin (1B) was 0.03 mass%. Therefore, the amount of the metal chelating agent (A) used in Example 1 was 3.7 times the total amount of the polyvalent metal cations.

[0213] In Example 1, the amount of the metal chelating agent (A) used was 0.11% by mass relative to 100% by mass of the recycled water absorbent resin (1B).

[0214] [Example 2] In the grinding step of Comparative Example 1, when the filtrate after the dehydration treatment was put into the meat chopper to grind the gel, a chelating agent aqueous solution consisting of 0.2 parts by mass of trisodium diethylenetriaminepentaacetate and 4 parts by mass of deionized water was continuously put into the meat chopper relative to 100 parts by mass of the solid content of the filtrate. The dehydration step, pulverization step, classification step, and surface cross-linking step were carried out in the same manner as in Comparative Example 1. By these operations, a surface-cross-linked recycled water absorbent resin (2A) containing 2000 ppm of a metal chelating agent (metal chelating agent (A)) was obtained.

[0215] Then, 100 parts by mass of the recycled water absorbent resin (2A) was uniformly mixed with an aqueous solution of the metal chelating agent (A) consisting of 0.01 part by mass of trisodium diethylenetriaminepentaacetate (A) and 1 part by mass of deionized water, and then dried at 60°C for 1 hour.

[0216] Thereafter, the obtained dried product was cooled, and the cooled product was passed through a JIS standard sieve with a mesh size of 710 μm to obtain a recycled water absorbent resin (2B). The obtained recycled water absorbent resin (2B) had a CRC of 36.0 g / g, an AAP0.3 of 28.9 g / g, a YI value (yellowness index) of 14.7, a water soluble content of 15 mass%, and a water absorption rate (Vortex) of 49 seconds. Table 2 shows the results of various measurements and evaluations of the recycled water absorbent resin (2B).

[0217] In Example 2, the amount of polyvalent metal cations in the finally obtained recycled water absorbent resin (2B) was 0.03% by mass. Therefore, the amount of the metal chelating agent (A) used in Example 2 was 7.0 times by mass relative to the total amount of the polyvalent metal cations.

[0218] In Example 2, the amount of the metal chelating agent (A) used was 0.21% by mass relative to 100% by mass of the recycled water absorbent resin (2B).

[0219] [Example 3] In Example 1, the aqueous solution of the metal chelating agent (A) added after the surface cross-linking step was changed to an aqueous solution of an inorganic reducing agent consisting of 0.02 parts by mass of sodium sulfite, which is an inorganic reducing agent, and 1 part by mass of deionized water (addition step (B) was carried out), and the same operation as in Example 1 was performed to obtain a recycled water absorbent resin (3B). The obtained recycled water absorbent resin (3B) had a CRC of 36.2 g / g, an AAP0.3 of 29.0 g / g, a YI value (yellowness index) of 15.5, a water-soluble content of 15 mass%, and a water absorption rate (Vortex) of 50 seconds. Table 2 shows the results of various measurements and evaluations of the recycled water absorbent resin (3B).

[0220] In Example 3, the amount of polyvalent metal cations in the finally obtained recycled water absorbent resin (3B) was 0.03 mass%. Therefore, the amount of the metal chelating agent (A) used in Example 3 was 3.3 times the total amount of the polyvalent metal cations.

[0221] In Example 3, the amount of the metal chelating agent (A) used was 0.10% by mass with respect to 100% by mass of the recycled water absorbent resin (3B).

[0222] [Table 2]

[0223] (summary) The recycled water-absorbent resin (C1) of Comparative Example 1 has a poor (large) YI value (Yellow-Index) and a yellowish color, which reminds of urine remaining, and is undesirable from the viewpoint of hygiene. Therefore, in Comparative Examples 2 and 3, 0.05% by mass (Comparative Example 2) and 3.0% by mass (Comparative Example 3) of bleaching agent were added when drying the hydrogel. As a result, in Comparative Example 2, there is yellowing, the YI value is high, that is, the color tone is not improved, and it is understood that the amount of bleaching agent used is insufficient. On the other hand, in Comparative Example 3, since a large amount of bleaching agent was used, the YI value became small and the product became white, that is, the color tone was improved, but since the bleaching agent itself is also a decomposition agent for the water-absorbent resin, it is understood that the recycled water-absorbent resin has poor water-soluble content and poor durability. That is, if the amount of bleaching agent used is small, the color tone is not improved, whereas if the amount of bleaching agent used is large enough to improve the color tone (i.e., to exhibit a sufficient bleaching effect), the water absorbent resin has poor water-soluble matter and is poor in durability.

[0224] As shown in Examples 1 to 3, by using a metal chelating agent instead of a bleaching agent, the color tone became almost white with a clean feeling, that is, a recycled water absorbent resin was obtained that was excellent in color tone, water-soluble content, and durability. Moreover, the water absorption speed was also improved in Examples 1 to 3. Furthermore, in Examples 1 to 3, the use of the metal chelating agent improved the deodorizing effect of the recycled water absorbent resin.

[0225] From the above, it is understood that the addition of a metal chelating agent can solve the various problems (coloration, decrease in water absorption rate, deterioration, etc.) of conventional recycled water absorbent resins. [Industrial Applicability]

[0226] According to one aspect of the present invention, a method for producing a recycled water-absorbent resin can be provided, which can provide a recycled water-absorbent resin that is excellent in color tone, water-soluble content, and durability. Also, according to one aspect of the present invention, a method for producing a water-absorbent resin using the recycled water-absorbent resin as a part of a raw material for the water-absorbent resin can be provided. The recycled water-absorbent resin and the water-absorbent resin can be suitably used for various applications, particularly for sanitary products such as paper diapers, sanitary napkins, and adult incontinence products.

Claims

1. A method for producing a recycled water-absorbent resin from a water-absorbent resin recovered from used absorbent articles and / or waste generated in a process for producing a water-absorbent resin, comprising the steps of: A washing step of washing the water absorbent resin and / or a dehydration step of dehydrating the water absorbent resin; An addition step (A) of adding a metal chelating agent (A) (excluding a monovalent carboxylic acid (salt) consisting of only CHO and a polyvalent carboxylic acid (salt) consisting of only CHO) to the water absorbent resin; and A drying step of drying the water absorbent resin, The method for producing a recycled water absorbent resin, wherein the adding step (A) is carried out after the washing step and / or the dehydrating step.

2. The method for producing a recycled water-absorbing resin according to claim 1, wherein the water-absorbing resin is a water-absorbing resin recovered from one or more types of used absorbent articles and / or waste generated in a manufacturing process of one or more types of the water-absorbing resin.

3. The method for producing a recycled water-absorbent resin according to claim 1, wherein the water-absorbent resin recovered from the used absorbent article and / or waste generated in the process of producing the water-absorbent resin contains a metal chelating agent (B).

4. The method for producing a recycled water absorbent resin according to claim 1, wherein the metal chelating agent (A) is (i) a polyvalent phosphoric acid (salt) having a plurality of nitrogen atoms, and / or (ii) a polyvalent carboxylic acid (salt) other than a polyvalent carboxylic acid (salt) consisting only of CHO, and is a polyvalent carboxylic acid (salt) having a plurality of nitrogen atoms.

5. The method for producing a recycled water absorbent resin according to claim 1, further comprising an addition step (B) of adding an inorganic reducing agent to the water absorbent resin after the washing step and / or the dehydration step.

6. The method for producing a recycled water absorbent resin according to claim 1, wherein the water absorbent resin recovered from the used absorbent article and / or the waste generated in the production process of the water absorbent resin contains one or more polyvalent metal cations selected from the group consisting of calcium ions, magnesium ions, and aluminum ions.

7. The method for producing a recycled water absorbent resin according to claim 6, wherein the amount of the metal chelating agent (A) used is 2 times or more and 1000 times or less by mass relative to the total mass of the polyvalent metal cations in the recycled water absorbent resin.

8. The method for producing a recycled water absorbent resin according to any one of claims 1 to 7, wherein the amount of the metal chelating agent (A) used is 0.01 mass% or more and 2.00 mass% or less with respect to 100 mass% of the recycled water absorbent resin.

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