JP2014110845A - Absorbent composite - Google Patents

Abstract

PROBLEM TO BE SOLVED: To provide a composite for constituting an absorber excellent in an absorption rate, a dry feeling after absorption, absorption property of a protein-containing solution by improving the wettability of absorbent resin and preventing gel blocking in the order of particles, an absorption sheet using the composite, an absorbent article using the absorption sheet, and manufacturing methods thereof.SOLUTION: A composite includes hydrophilic fiber and acid radical. Part of the acid radical is composed of absorbent resin neutralized by an alkali metal salt and an ammonium salt. The hydrophilic fiber and the absorbent resin are directly bonded to each other.

Description

  The present invention relates to a composite composed of a hydrophilic fiber and a composite salt-type absorbent resin, an absorbent sheet, an absorbent article, and a method for producing them.

  In recent years, an absorbent resin that gels by absorbing a large amount of water has been developed and used mainly in the field of sanitary materials such as disposable diapers and sanitary napkins. Absorbent resins are usually fine powders and have the disadvantage of poor handling, and in the field of sanitary materials such as disposable diapers, they are mixed with pulp and used in bags. Pulp has a role of supporting the absorbent resin and a role of preventing gel blocking that the absorbent resins come into contact with each other to prevent liquid passage. However, since the absorbent resin and the pulp have different specific gravities, the absorbent resin and the pulp are easily separated, and there is a problem in that the internal resin is biased, gel blocking cannot be suppressed, and it is difficult to exhibit the absorption performance uniformly. In addition, there is a problem that the required pulp amount is large and the thickness is increased. Furthermore, these methods require the use of relatively long fiber pulp to immobilize the absorbent resin, and the milling conditions are difficult and the productivity is poor, and the finely pulverized pulp is lost in the process. There is a problem that the use efficiency of the material becomes poor.

In order to solve such problems, it has been studied to use an absorbent body in which a powdery absorbent resin is fixed to a sheet and molded into a sheet shape. The following methods are known as methods for forming a sheet.
For example, in patent document 1, in order to fix an absorptive resin and to make a sheet | seat, the absorptive resin is combined using the heat-meltable adhesive agent.
In Patent Document 2, a mixture of pulverized pulp and thermoplastic fibers is heat-treated to form a sheet, and an absorbent resin powder solid is supported thereon.
Patent Document 3 discloses a method in which an adhesive component in an absorbent resin is used and the wet pulp and the absorbent resin are fixed while being dried.

Patent Document 4 discloses an example in which an absorbent resin and a fibrous material such as pulp are uniformly mixed and hydrogen bonds between pulps are formed using water to form a sheet.
In patent document 5, the absorptive polymer particle in progress of polymerization is made to adhere to a fibrous base material, and the absorptive resin is polymerized on the fibrous base material.
Patent Document 6 discloses an absorbent sheet that directly binds an absorbent resin to a hydrophilic base material, thereby creating a water passage from the base material to the absorbent resin and exhibiting a high absorption capacity of the absorbent resin itself. It is disclosed. Patent Document 7 discloses a composite in which hydrophilic fibers are directly bonded to an absorbent resin to increase the passage of moisture to the absorbent resin and suppress blocking.

Japanese Patent No. 3196933 Japanese Patent Laid-Open No. 53-4789 JP-A-56-60556 Special table 2003-508647 gazette JP 2003-11118 A International Publication No. 2006/121148 International Publication No. 2011/158838

However, in these sheet structures, the absorbent resin swelling space is not sufficiently secured and gel blocking cannot be prevented, and the absorbent resin has poor wettability. No satisfactory one was obtained. In addition, in liquids containing proteins such as milk and blood, the gel blocking phenomenon between absorbent resins becomes prominent, and because proteins adhere to the absorbent resin surface and block absorption, those that can absorb these liquids It did not exist.
The present invention improves the wettability of the absorbent resin, prevents gel blocking in the order of the particle internal structure, and further the internal structure of the particle, thereby improving the absorption rate, the dry feeling after absorption, and the liquid containing protein and the like. It is an object of the present invention to provide a composite for constituting an absorbent body that can absorb water, an absorbent sheet using the composite, an absorbent article using the absorbent sheet, and a method for producing the same.

  As a result of intensive studies on the above problems, the present inventors have found that the surface layer of the absorbent resin is thinly crosslinked in the composite in which the hydrophilic fiber and the absorbent resin containing an acid group are directly bonded. As a result, it is difficult for gel blocking between particles and particles to occur regardless of the form used, and also exhibits high wettability and high suction force. It has been found that it is excellent, in particular, the absorption characteristics of a liquid containing a protein that is prone to blocking.

  In addition, it includes a step of dehydrating and drying from a mixed state of hydrophilic fiber, absorbent resin, and water, a step of adding a compound having two or more functional groups capable of reacting with acid groups, and a crosslinking step by heating. And found that an ideal composite was formed. In addition, by adhering the composite to the substrate with an adhesive, or by mixing and fusing the composite with thermoplastic fibers, it is possible to form a thin absorbent sheet that maximizes the properties of the composite. I found it.

  Furthermore, the present inventors have found that the absorbent sheet can be used as it is as an absorbent article simply by attaching an auxiliary member to the absorbent sheet, and a resource-saving absorbent article can be formed with few used members. Moreover, since this absorbent article can be manufactured in the same line as an absorption sheet manufacturing process, it discovered that it could manufacture with high productivity.

That is, this invention is the following composites, an absorbent sheet, an absorbent article, and their manufacturing methods.
[1]
A composite comprising hydrophilic fibers and an absorbent resin and having the following characteristics.
(1) The hydrophilic fiber and the absorbent resin are directly bonded.
(2) The absorbent resin is surface-crosslinked.
[2]
The composite according to the above [1], wherein the absorbent resin has an acid group.
[3]
The composite according to [1] above, wherein the surface of the absorbent resin is hydrophobic.
[4]
The manufacturing method of the composite material comprised from the absorptive resin which has a hydrophilic fiber and an acid group including the following process.
(A) A step of bringing a hydrophilic fiber and an absorbent resin into contact and dehydrating and drying the hydrophilic fiber and the absorbent resin in the presence of water to obtain a composite precursor.
(B) A step of adding a compound having two or more functional groups capable of reacting with an acid group to the composite precursor.
(C) A step of performing a crosslinking reaction with the compound by heating.
[5]
The method for producing a composite as described in [4] above, wherein the surface strength of the absorbent resin before dehydration drying is 0.1 to 5.5 N.
[6]
The method for producing a composite as described in [4] or [5] above, wherein the steps (B) and (C) are carried out with a water content of 20% or less based on the weight of the water absorbent resin. .
[7]
An absorbent sheet, wherein the composite according to any one of [1] to [3] is adhered to a substrate with an adhesive.
[8]
An absorbent sheet comprising the composite according to any one of [1] to [3] above and a thermoplastic fiber, wherein the thermoplastic fiber is formed into a sheet by heat-sealing.
[9]
Forming the sheet by bringing the composite according to any one of [1] to [3] above into contact with a thermoplastic fiber and heating with hot air at a wind speed of 0.1 to 100 m / s and a temperature of 70 ° C to 180 ° C. The manufacturing method of the absorption sheet characterized by this.
[10]
An absorbent article comprising the absorbent sheet according to the above [7] or [8] and an auxiliary member.
[11]
The method for manufacturing an absorbent article according to the above [10], wherein the manufacturing process of the absorbent sheet and the mounting process of the auxiliary member are performed on the same line.

According to the present invention, it is possible to provide a composite that is excellent in absorption rate and dry feeling after absorption and that also absorbs a liquid containing a protein. The composite is less susceptible to gel blocking by any method of use and exhibits high wettability, so that it can be suitably used for sanitary materials and the like. In particular, since it has excellent absorption characteristics of protein-containing liquids, it can be suitably used for breast milk pads, loose stool absorbents, sanitary products, surgical sheets and the like.
In addition, since the composite does not require a material for preventing gel blocking, the number of members used in the sanitary material can be reduced, which contributes to simplification of the manufacturing process of sanitary material and resource saving. it can. Since the absorbent sheet of the present invention exhibits a high absorption rate while being thin, it can reduce the risk of leakage.

1 is an overall view of a stretchable nonwoven fabric. It is a figure which shows the manufacturing process of an elastic nonwoven fabric. It is an enlarged view of die opening. It is sectional drawing of a composite fiber. It is a top view of an elastic composite fiber. It is an optical micrograph of a composite.

  Hereinafter, embodiments of the present invention will be described in detail. In addition, this invention is not limited to the following embodiment, It can implement by changing variously within the range of the summary.

<Composite>
The composite of the present invention is composed of a hydrophilic fiber and an absorbent resin having an acid group, both of which are directly bonded, and the absorbent resin is surface-crosslinked. Although the hydrophilic fiber has a high speed of temporarily capturing the liquid, the liquid is released when pressure is applied. On the other hand, the absorbent resin has a low absorption rate, but can completely take in the liquid and retain the liquid even when pressure is applied.

  The composite of the present invention has a high absorption rate and an excellent dry feeling. This is presumably because the liquid captured by the hydrophilic fibers can be quickly fed into the absorbent resin. In particular, liquids that are difficult to be absorbed by absorbent resins that contain proteins can also be absorbed by the composite. This is considered because it can be forcibly fed into the absorbent resin through the hydrophilic fiber.

  In the composite of the present invention, the hydrophilic fiber prevents contact between the absorbent resins and prevents the formation of gel blocking that inhibits the swelling of the absorbent resin. Moreover, an absorption speed | rate can be raised because a hydrophilic fiber becomes a water passage and conveys a liquid to an absorptive resin.

  In order to increase the absorption rate by the above mechanism, it is essential that the hydrophilic fiber and the absorbent resin are directly bonded without using an adhesive or the like. When bonded using an adhesive, the adhesive prevents the liquid from being transported from the hydrophilic fiber to the absorbent resin, so that the effect of increasing the absorption rate cannot be obtained. The form of direct adhesion is not particularly limited, but for example, a form in which hydrophilic fibers are incorporated into the surface or inside of the absorbent resin, hydrogen bonds or chemical bonds between the absorbent resin and the hydrophilic fibers. It is preferable. From the viewpoint of improving the absorption rate by transporting the liquid from the hydrophilic fiber to the absorbent resin, it is most preferable that the adhesive is bonded in a form in which the hydrophilic fiber is taken into the surface or inside of the absorbent resin.

  The bonded form can be confirmed by observing with an optical microscope or the like. Further, when the composite is washed with an organic solvent in which the adhesive dissolves, it can be confirmed whether or not it is direct adhesion depending on whether or not the hydrophilic fiber and the absorbent resin are detached. In the case where the hydrophilic fiber and the absorbent resin are directly bonded, the hydrophilic fiber and the absorbent resin are not detached by washing.

  The form in which the hydrophilic fiber is taken into the surface or inside of the absorbent resin can be realized, for example, by dehydrating and drying the absorbent resin and the hydrophilic fiber in the presence of water. The concept of using hydrophilic fibers in the liquid passage has been around for a long time, but none of them had a great effect in terms of absorption speed, especially in terms of quick absorption of difficult-to-absorb liquids including proteins. .

  In the present invention, it is necessary that the absorbent resin is surface-crosslinked in order to facilitate the exchange of liquid between the hydrophilic fiber and the absorbent resin. The surface layer in the present invention means the outer surface of the absorbent resin and / or the vicinity of the interface in the absorbent resin between the absorbent resin and the hydrophilic fiber. That is, the surface layer crosslinking means that a part of the acid groups in the surface layer portion of the absorbent resin is crosslinked by a compound having two or more functional groups capable of reacting with the acid groups. Surface cross-linking can be realized, for example, by adding a compound having two or more functional groups that react with acid groups to a composite composed of hydrophilic fibers and an absorbent resin in advance, followed by heat cross-linking. Although it is effective to crosslink to suppress the blocking phenomenon, it is surprising that only the surface layer is cross-linked rather than thickly cross-linked, such as normal absorption of protein-containing liquids and high-viscosity liquids. The present inventors have found that it is possible to absorb liquids that cannot be absorbed by the functional resin alone. As described in Patent Document 7, when a composite is produced by dehydration drying using an absorbent resin containing a crosslinking agent on the surface of the absorbent resin in advance, the crosslinking agent is brought into the resin together with water. Since it permeates, not only the surface layer portion but also a thick cross-linked layer is formed. Therefore, it is difficult to absorb a liquid containing a protein or a hardly absorbable liquid such as a high viscosity liquid. The reason for this is unknown, but when the composite absorbs a hard-to-absorb liquid, it is made not through the surface of the absorbent resin, but through the hydrophilic fibers that adhere to the absorbent resin. It is expected that cross-linking other than the surface of the absorbent resin that is in contact and the interface is not necessary, but rather the molecular mobility of the composite as a whole is lowered, so that the moving speed of the liquid in the fiber is lowered.

  It is preferable that the surface of the absorbent resin in the composite is hydrophobized. Usually, it is not preferable that the surface of the absorbent resin is hydrophobized because it prevents liquid absorption. However, in the case of the composite of the present invention, absorption is performed through hydrophilic fibers, so the surface of the absorbent resin itself is hydrophobic. It does not affect absorption even though On the other hand, it is preferable that the surface of the absorbent resin is hydrophobized, so that blocking between the resins is less likely to occur, and adhesion of an absorption inhibitor such as a protein can be prevented. Any method may be used to hydrophobize the surface of the absorbent resin in the composite, for example, a hydrophobic substance may be added during and / or after the manufacture of the composite, If the absorbent resin has an acid group, a hydrophobic substance such as a hydrocarbon or a silicone-based substance having a functional group capable of reacting with the acid group may be allowed to react with the surface. Hydrophobic surfactants or the like that may be added may be added. A liquid compound may be added, or a solid substance capable of creating a physically hydrophobic space may be added.

  From the viewpoint of the absorption amount of the absorbent resin, 10-100% of the acid groups of the absorbent resin are preferably neutralized, more preferably 20-90% neutralized, more preferably 30-80% More preferably, it is neutralized, most preferably 40-75% neutralized.

  The mass ratio of the hydrophilic fiber to the absorbent resin is preferably 1: 5 to 2: 1, more preferably 1: 4 to 1: 1, and further preferably 1: 3 to 7:10. A ratio of 2: 5 to 3: 5 is most preferable. It is preferable that the mass ratio of the hydrophilic fibers is 1/6 or more because the probability that the absorbent resins come into contact with each other can be reduced and the absorption rate can be increased. It is preferable for the mass ratio of the hydrophilic fibers to be 2/3 or less because a dry feeling can be obtained upon absorption of the composite.

  The mass ratio of the hydrophilic fiber and the absorbent resin can be calculated by separating the absorbent resin and the hydrophilic fiber as appropriate from the composite that has been previously weighed and measuring the respective masses. . For example, in the case of an acrylic acid-based absorbent resin, the absorbent resin can be water-solubilized by applying ultraviolet rays in an absorbed state. If the absorbent resin is water-solubilized, the hydrophilic fibers can be separated by filtration or the like. A suitable separation method may be taken according to the type of hydrophilic fiber and absorbent resin to be used. It is preferable from the viewpoint of efficiently using the raw material that the composite is previously produced using hydrophilic fibers and an absorbent resin having a predetermined mass ratio.

  The apparent bulk density and the bulk specific gravity after compression of the composite are preferably 1: 2 to 1:10, more preferably 4: 9 to 1: 7, and 2: 5 to 1: 5. It is more preferable that the ratio is 4:11 to 1: 4. In the present invention, the apparent bulk specific gravity refers to the mass per volume of the absorbent resin particles and the interparticle voids in a state where no load is applied. Specifically, an appropriate amount of the composite is placed in a graduated cylinder, covered with a lid, shaken up and down about 10 times, and left for about 10 minutes. Thereafter, the volume is read, the mass is measured, and the mass is calculated by dividing the mass by the volume.

On the other hand, the bulk specific gravity after compression represents the mass per volume of the particles of the absorbent resin and the interparticle voids in a state where a weight is applied. The bulk specific gravity after compression is as follows. Put an appropriate amount of composite in a graduated cylinder, cover it for 10 times, cover it for about 10 minutes, leave it for about 10 minutes, and then apply a load of 5 kg / cm ² for 10 minutes. Measure and calculate. These measurements are performed at 23 ° C. and a relative humidity of 30% RH.

  The ratio between the apparent bulk specific gravity and the bulk specific gravity after compression is an index of how much space can be secured around the absorbent resin. Of the ratio of the apparent bulk density to the compressed bulk specific gravity, the ratio of the apparent bulk specific gravity is 1/3 or more, so that a sufficient space can be secured around the absorbent resin and gel blocking can be prevented. On the other hand, if the ratio of the apparent bulk specific gravity to the bulk specific gravity after compression is 1/11 or less, it can be produced without deteriorating the handleability in the production process.

  In the composite of the present invention, the coverage of the absorbent resin is preferably 80% or more, more preferably 90% or more, further preferably 95% or more, and 99% or more. Most preferred. The coverage can be calculated by enlarging the range of 100 μm to 300 μm and taking a photograph of the composite, and dividing the area of the absorbent resin portion in the photograph by the area of the fiber portion. The photograph can be used with an optical microscope or an electron microscope, which can easily distinguish between the absorbent resin and the hydrophilic fiber. Taking 10 fields of view for each composite while changing the angle and the measurement site, the same measurement is performed, and the average value of 10 times is defined as the coverage. Higher coverage is preferable because gel blocking between absorbent resins can be efficiently suppressed.

  The hydrophilic fiber of the present invention preferably has an average particle size of 10-200 μm, more preferably 20-120 μm, still more preferably 30-80 μm, still more preferably 35-55 μm. 40-50 μm is most preferable. If the average particle size is too small, the possibility that the absorbent resins come into contact with each other increases and blocking may occur. On the other hand, if the average particle diameter is too large, the entanglement between the fibers becomes too large, and the liquid permeability in the fibers may be reduced, and the handleability of the composite may be reduced.

  The average particle diameter of the hydrophilic fiber can be measured using a laser diffraction / scattering particle size distribution measuring apparatus. In the measurement, hydrophilic fibers dispersed in water as a dispersion medium are treated with ultrasonic waves for 1 minute, and the volume-based median diameter at 25 ° C. is measured. The shape of the hydrophilic fiber used in the present invention is not limited as long as the average particle diameter can be measured by the above method. That is, the hydrophilic fiber does not need to be in the form of particles, and may be in the shape of a rod, scale, needle, string, or the like.

  Although the average particle diameter of the hydrophilic fibers can be adjusted during the process of producing the composite, it is preferable to use hydrophilic fibers whose average particle diameter has been adjusted in advance. The average particle diameter of the hydrophilic fibers in the composite can be measured by separating the hydrophilic fibers and the absorbent resin by an appropriate method. For example, in the case of an acrylic acid-based absorbent resin, the absorbent resin can be water-solubilized by applying ultraviolet rays in an absorbed state. If the absorbent resin is water-solubilized, the hydrophilic fibers can be separated by filtration or the like. A suitable separation method may be taken according to the type of hydrophilic fiber and absorbent resin to be used.

Examples of the acid group in the absorbent resin include a carboxyl group and a sulfonic acid group, and a carboxyl group is preferable. Examples of the functional group that reacts with the acid group include a hydroxyl group, an epoxy group, and an amino group. Examples of the compound having two or more functional groups that react with the acid group include polyhydric alcohols, polyhydric amines, polyhydric epoxides, and polyhydric epoxides and / or polyhydric alcohols from the viewpoint of absorption rate. Preferably there is.
It is preferable to combine the composite of the present invention with a material other than the hydrophilic fiber and the absorbent resin. For example, it is preferable to combine with a surfactant, a deodorizing agent or the like.

(Hydrophilic fiber)
When the particle size of the hydrophilic fiber in the present invention is measured with a sieve according to JIS Z 8901, it is preferable to pass through a sieve having an opening of 355 μm in an amount of 50% by mass or more, more preferably 70% by mass or more, and 80% by mass. % Is more preferable, and 90% or more is most preferable. Moreover, it is preferable to pass 50 mass% or more through a sieve having an opening of 300 μm, more preferably 70 mass% or more, more preferably 80 mass% or more, and most preferably 90 mass% or more. preferable. When the particle size of the hydrophilic fibers is large, the hydrophilic fibers are easily entangled with each other.

  The hydrophilic fibers in the present invention preferably have an apparent bulk specific gravity of 0.05 to 0.65 g / ml, more preferably 0.1 to 0.55 g / ml, and 0.15 to 0.005. More preferably, it is 45 g / ml, and most preferably 0.2-0.35 g / ml. The apparent bulk specific gravity of the hydrophilic fiber is 0.05 to 0.65 g / ml, an appropriate size space is formed around the absorbent resin, and the hydrophilic fiber is water-permeable and wettable to the absorbent resin. The absorption rate is improved. The apparent bulk specific gravity can be measured by the same method as the apparent bulk specific gravity of the composite.

  In the present invention, it is preferable to use a cellulose-based hydrophilic fiber as the hydrophilic fiber. Cellulose-based hydrophilic fibers represent fibers made mainly of cellulose. Cellulose may be derivatized by treatment such as esterification or etherification. Moreover, what was mixed with the other fiber may be used.

  Examples of cellulose include cotton, hemp, rayon, polynosic, lyocell, cupra, and pulp. Of these, pulp is preferable. The pulp may be wood pulp or non-wood pulp. In wood pulp, coniferous trees or hardwood trees may be used. Examples of non-wood pulp include bagasse, grass, straw and bamboo. Moreover, although it can also recycle | regenerate from waste paper etc. to make a pulp, when using for a sanitary material, it is preferable that it is a virgin pulp manufactured directly from wood etc.

  In sanitary materials, pulp is widely used for the purpose of entanglement with an absorbent resin and for enhancing the trapping ability of liquids. Usually, pulp raw materials are pulverized and used as fibers. In order to efficiently carry the absorbent resin by utilizing the entanglement between the fibers, a long fiber of about 10 to 13 mm is preferably used. However, even if pulverization is performed using such a long fiber length as a target, a fine powder unsuitable for use is also generated. Since this fine powder is a problem because it is diffused and lost in the sanitary material manufacturing process, it is preferable to use pulp with a small particle diameter that causes loss. The pulverization using this region as a target can be performed with a simpler apparatus than that using a long fiber as a target, and the particle size distribution can be narrowed. For this reason, when using pulverized pulp, the use of pulp having a small particle diameter has the advantage that the loss rate of the pulp is reduced and the productivity is increased.

In the absorbent sheet, the amount of the hydrophilic fiber, it is preferable to be 10 to 150 g / m ^2, more preferably from 20 to 100 g / m ^2, more preferably from 30 to 80 g / m ^2, Most preferably, it is 40-60 g / m < ² >. If it is less than 10 g / m ² , the absorption rate may be inferior, and if it is more than 150 g / m ² , the dry feeling may be inferior.

(Absorbent resin)
The average particle size of the absorbent resin in the present invention is preferably 20 to 500 μm, more preferably 40 to 400 μm, still more preferably 60 to 300 μm, still more preferably 80 to 275 μm, and most preferably 100 to 250 μm. . If the average particle diameter is too large, the surface area per unit mass of the absorbent resin is reduced, and therefore, the contact surface with the hydrophilic fiber is reduced, and it may be difficult to obtain the effect of improving the absorption rate. If the average particle size is too small, it may be difficult to obtain a dry feeling because of poor absorption performance.

  In this specification, the average particle diameter of the absorbent resin is determined as follows. The opening of the absorbent resin is 20 μm, 25 μm, 32 μm, 38 μm, 45 μm, 53 μm, 63 μm, 75 μm, 90 μm, 106 μm, 212 μm, 300 μm, 425 μm, 500 μm, 600 μm, 710 μm, 850 μm, 1000 μm, 1180 μm, 1400 μm, 1700 μm, Sift using a 2500 μm sieve. The particle diameter is an intermediate value between the opening of the sieve that can pass and the opening of the sieve that cannot pass. For example, the particle diameter of the absorbent resin that can pass through a 25 μm sieve and cannot pass through a 20 μm sieve is 22.5 μm. For each particle size, the product of the particle size and the mass ratio of the particle size in the entire absorbent resin is determined, and the sum of all of them is calculated as the average particle size. In addition, about what passed the 20 micrometers sieve, it is set to 10 micrometers, and about what remained on the 2500 micrometers screen, it shall be 2700 micrometers.

  The particle size is not particularly limited, but a particle size of 10 μm or more is preferable because the generation of fine powder is often a problem in handling the absorbent resin. More preferably, it is 30 micrometers or more, More preferably, it is 50 micrometers or more. The classification of the absorbent resin can be achieved timely using, for example, a sieve. The shape of the absorbent resin is not particularly limited, but is preferably particulate. There are no particular limitations on the spherical shape by suspension polymerization, the irregular shape obtained by crushing the aqueous solution polymer, the porous shape for increasing the specific surface area, the shape in which a plurality of spherical particles are aggregated, and the like.

  Further, in the absorbent resin, the particles that can pass through a sieve having an opening of 90 μm are preferably 50% by mass or less, more preferably 30% by mass or less, and still more preferably 10% by mass or less. . Moreover, it is preferable that it is 50 mass% or less, and, as for the particle | grains which cannot open the sieve of 425 micrometers, it is more preferable that it is 30 mass% or less. Furthermore, it is preferable that the particle | grains which cannot open a sieve with an opening of 300 micrometers are 70 mass% or less, It is more preferable that it is 50 mass% or less, It is still more preferable that it is 30 mass% or less. When an absorbent resin having such a relatively sharp particle size distribution is used, a uniform composite can be easily formed, and the subsequent handleability is excellent.

  In the absorbent resin in the present invention, the residual monomer concentration with respect to the total amount of the absorbent resin is preferably 200 mass ppm (hereinafter also referred to simply as “ppm”) or less, more preferably 100 ppm or less, and 50 ppm or less. More preferably, it is more preferably 10 ppm or less. When there are many residual monomers, there are many elution components at the time of liquid absorption, and it is unpreferable from a viewpoint of absorption rate and absorption amount.

  The residual monomer concentration in the absorbent resin material before production of the composite is preferably 5% or less, more preferably 1% or less, further preferably 0.1% or less, 0.05% It is still more preferable that it is below, and it is most preferable that it is 0.03% or less. Residual monomers can also be reduced by completing the polymerization by heat treatment during the manufacture of the composite or after completion. If an absorbent resin with a large amount of residual monomer is used as a starting material, it is difficult to complete the polymerization reaction of the residual monomer at the time of producing the composite, and a large amount of residual monomer tends to remain in the end, which is not preferable. Further, depending on the reaction method, the texture may be impaired, which is not preferable. For this reason, in the present invention, it is preferable to use a prepolymerized absorbent resin.

  The amount of residual monomer can be quantified using the following method. The absorbent resin is added to 0.9% physiological saline of 250 times the mass of the absorbent resin, extracted for about 6 hours with stirring at room temperature, and then filtered. The filtrate is quantified using a liquid chromatography method.

  In the present invention, the type of the absorbent resin is not particularly limited, and any absorbent resin may be used, but an absorbent resin having an acid group in the side chain is preferable, and an absorption having a carboxyl group in the side chain. More preferably, it is a functional resin. The carboxyl group-containing unit is derived from monomers such as acrylic acid, methacrylic acid, itaconic acid, maleic acid, crotonic acid, fumaric acid, sorbic acid, cinnamic acid, their anhydrides and neutralized salts thereof. Units.

  An absorbent resin having an acid group in the side chain is preferable because an electrostatic repulsion between the acid groups occurs during liquid absorption and the absorption speed increases. It is preferable that the acid group is neutralized because the liquid is absorbed into the absorbent resin by osmotic pressure, and it is preferable because it is easily bonded directly to the hydrophilic fiber by the salt.

  The absorptive resin may have a unit that does not contain an acid group. Examples include acrylamide, methacrylamide, N-ethyl (meth) acrylamide, Nn-propyl (meth) acrylamide, N- Isopropyl (meth) acrylamide, N, N-dimethyl (meth) acrylamide, 2-hydroxyethyl (meth) acrylate, 2-hydroxypropyl (meth) acrylate, methoxypolyethylene glycol (meth) acrylate, polyethylene glycol mono (meth) acrylate, Hydrophilic units derived from nonionic compounds such as N-vinylpyrrolidone, N-acryloylpiperidine, N-acryloylpyrrolidine, (meth) acrylonitrile, styrene, vinyl chloride, butadiene, isobutene, ethylene, propylene, Allyl (meth) acrylate, lauryl (meth) hydrophobic units derived from compounds such as acrylate.

  The absorbent resin may contain a unit that becomes a polymerizable crosslinking agent between polymer molecular chains. For example, diethylene glycol diacrylate, N, N′-methylenebisacrylamide, polyethylene glycol diacrylate, polypropylene glycol diacrylate, trimethylolpropane diallyl ether, allyl glycidyl ether, pentaerythritol triallyl ether, pentaerythritol diacrylate monostearate, bisphenol Examples thereof include units derived from diacrylate, isocyanuric acid diacrylate, tetraallyloxyethane, diallyloxyacetate, and the like.

  The absorbent resin may contain a compound having two or more functional groups that react with an acid group, or the absorbent resin may have a functional group that reacts with an acid group. . Examples of the compound having two or more functional groups that react with the acid group include ethylene glycol diglycidyl ether, trimethylolpropane triglycidyl ether, (poly) glycerin polyglycidyl ether, diglycerin polyglycidyl ether, and propylene glycol diglycidyl. Glycidyl ether compounds such as ethers; polyvalents such as (poly) glycerin, (poly) ethylene glycol, propylene glycol, 1,3-propanediol, polyoxyethylene glycol, triethylene glycol, tetraethylene glycol, diethanolamine, triethanolamine Examples of alcohols include polyvalent amines such as ethylenediamine, diethylenediamine, polyethyleneimine, and hexamethylenediamine. From the viewpoint of easy control of the reaction rate, polyhydric alcohols are preferred. In addition, polyvalent ions such as zinc, calcium, magnesium, and aluminum can be preferably used because they react with the acid group of the absorbent resin and act as a crosslinking agent. When the absorbent resin has a functional group that reacts with an acid group, examples of the functional group that reacts with an acid group include a hydroxyl group, an epoxy group, and an amino group.

  The addition ratio of the compound having two or more functional groups that react with the acid group and the polyvalent ions is preferably 0.1 to 10% by mass with respect to the absorbent resin, and 0.2 to 5% by mass. More preferably, it is more preferably 0.3 to 3% by mass, and most preferably 0.4 to 1% by weight.

  Examples of the absorbent resin include polyacrylic acid partial neutralized polymer cross-linked products (see, for example, JP-A-55-84304), and starch-acrylonitrile graft polymer hydrolysates (for example, JP-B-49-43395). ), Neutralized product of starch-acrylic acid graft polymer (for example, see JP-A-51-125468), saponified product of vinyl acetate-acrylic acid ester copolymer (for example, see JP-A-52-14689) ), Hydrolyzate of acrylonitrile copolymer or acrylamide copolymer (for example, see JP-B-53-15959), polyglutamate (for example, see JP-A-2003-192794), and the like. From the viewpoints of absorption performance, cost, etc., polyacrylate copolymers and polyacrylic acid partial neutralized polymer cross-linked products that are usually used for hygiene materials are preferred.

  Hereinafter, a polyacrylic acid polymer crosslinked product will be described as a preferred example of the absorbent resin to be used. In the polyacrylic acid polymer crosslinked product, preferably 50 mol% or more of the repeating units in the polymer molecular chain are carboxyl group-containing units. More preferably, it is 80 mol% or more, More preferably, it is 90 mol% or more. If the proportion of the carboxyl group-containing units in the repeating units is less than 50 mol%, the absorption performance may be inferior. The carboxyl group in the polymer molecular chain is preferably partially neutralized (partially neutralized). Examples of the salt include alkali metals such as sodium, potassium and lithium, and nitrogen-containing basic substances such as ammonia. . It is preferable that 30 mol% or more of the carboxyl group is neutralized, more preferably 50 mol% or more is neutralized, still more preferably 70 mol% or more is neutralized, and 90 mol% or more is neutralized. Most preferably.

  However, when using for a sanitary material, it is preferable that the ratio which is neutralized among the carboxyl groups which an absorptive resin has is 50-80 mol%. As the alkali metal salt, sodium, potassium and lithium are preferable, and sodium is most preferable. The amount of salt in the absorbent resin can be analyzed by ion chromatography after extraction with water, for example.

  It is preferable to have a distribution structure in which the neutralization rate of the carboxyl group at the center of the absorbent resin in the absorbent sheet is higher than the neutralization rate of the carboxyl group on the outer surface of the absorbent resin. The neutralization rate of the carboxyl group at the center of the absorbent resin is preferably 50 mol% or more, more preferably 60 mol% or more, most preferably 70 mol% or more, and the carboxyl group on the outer surface of the absorbent resin. Is preferably less than 50 mol%, more preferably 45 mol% or less, and most preferably 40 mol% or less. Moreover, it is preferable that the difference of the neutralization rate of an absorptive resin center part and an absorptive resin outer surface is 5 mol% or more, and it is still more preferable that it is 10 mol% or more. It is preferable that the neutralization rate of the carboxyl group in the central part of the absorbent resin is the above-mentioned numerical value, since the reduction in absorption capacity without pressure does not easily occur. Moreover, when the neutralization rate of the carboxyl group on the outer surface of the absorbent resin is the above-mentioned numerical value, it is preferable that the absorption capacity under pressure is difficult to decrease. However, when a volatile salt such as ammonia is contained, the ammonia is volatilized through a heating step or the like, so the ammonia neutralization rate of the carboxyl group tends to decrease and is not constant. The ammonia neutralization rate of the absorbent resin center and the outer surface of the absorbent resin is preferably within the above range in the final product.

  The higher the neutralization rate (also referred to as “surface salt concentration”) of the outer surface of the absorbent resin is, the higher the adhesive force with the hydrophilic fiber can be increased. In the step (before dehydration), the surface salt concentration is high, and it is preferable to reduce the surface salt concentration after bonding. Moreover, when manufacturing a composite by heat | fever dehydration, it is preferable that the surface salt concentration of the absorbent resin before a heating is high, and the surface salt concentration of the absorbent resin after a heating is made low. In addition, in this specification, salt concentration is synonymous with the neutralization rate of an acid group (carboxyl group).

  The outer surface of the absorbent resin refers to a portion exposed to the outside of the absorbent resin. Moreover, the said absorbent resin center part means the innermost part from the absorbent resin outer surface of the said absorbent resin. The absorbent resin preferably has a core-shell structure inside the absorbent resin, but the carboxyl group neutralization rate averaged over the entire absorbent resin is preferably 30 mol% or more, more preferably 50 mol%. That's it. If the average carboxyl group neutralization rate of the entire absorbent resin is extremely reduced, the absorption capacity may be reduced without pressure.

The neutralization rate of the absorbent resin can be determined by measuring the carboxyl group neutralization rate by the microscopic ATR method which is one of infrared absorption analysis methods.
The carboxyl group neutralization rate on the outer surface of the absorbent resin is measured directly by the microscopic ATR method. The measurement of the central part of the absorbent resin is carried out by the micro ATR method after cleaving the absorbent resin and exposing the central part by using, for example, an ultramicrotome (ULTRACUT N manufactured by Reichert). As the measuring apparatus, for example, FTS-575 manufactured by Bio-Rad may be used. As an index for defining the composition ratio of carboxylic acid and carboxylate, 1695 cm ⁻¹ (carboxylic acid ν _C═O baseline 1774 to 1616 cm ⁻¹ ) and 1558 cm ⁻¹ (carboxylate ν _{COO −} baseline 1616 to 1500 cm ⁻¹ ) The peak area ratio (1695/1558 cm ⁻¹ ) is calculated. Separately, partially polymerized crosslinked polyacrylic acid obtained by neutralizing 10 mol%, 30 mol%, 50 mol%, 70 mol%, 90 mol%, and 100 mol% of the total carboxylic acid with a salt was measured as a standard sample, and the composition ratio was determined from the prepared calibration curve. Ask.

Absorptive resin is so preferable that absorption performance is high, and in the measurement of the absorption capacity at the time of non-pressurization, it is preferred that the absorption capacity is 40 g / g or more, more preferably 45 g / g or more, and 50 g / g or more. More preferably. In the measurement of the water retention ratio, the water retention ratio is preferably 25 g / g or more, more preferably 29 g / g or more, still more preferably 33 g / g, and 39 g / g or more. Most preferred. Moreover, it is preferable that the absorption capacity under pressure at 57 g / cm ² is 10 g / g or more.

A higher absorption capacity of the absorbent resin is preferable because the amount of the absorbent resin to be used can be reduced. In the present specification, the absorption capacity of the absorbent resin refers to an amount capable of freely swelling and absorbing 0.9% physiological saline in a state where no load is applied to the absorbent resin. The absorption capacity of the absorbent resin is measured by the following method. Absorbent resin 0.05 g is uniformly placed in a non-woven tea bag bag (60 × 40 mm) and immersed in 0.9% physiological saline at 23 ° C. After 180 minutes, the bag is taken out, the corner of the tea bag is fixed, suspended for 10 minutes in an oblique state, drained, and then the mass is measured. The same operation is performed without using the absorbent resin, and the mass is measured to obtain a blank. The absorption rate is calculated according to (Equation 4). The measurement is performed three times, and the average value is taken as the absorption magnification.
(Equation 4) Absorption capacity of absorbent resin (g / g) = {(mass of tea bag after absorption) − (mass of blank tea bag after absorption) − (mass of absorbent resin)} / (absorption) Of the resin)

The absorption capacity under pressure of the absorbent resin of the present invention is measured by the following method. Put 0.02 g of absorbent resin into an acrylic resin cylinder with an inner diameter of 25 mm, a height of 30 mm, and a 250 mesh nylon nonwoven fabric at the bottom, and put a smoothly moving cylinder into the cylinder to make a measuring device and measure the mass. . A load of 278.33 g corresponding to 0.8 psi is placed on the upper part of the cylinder of the measuring device to obtain a load, which is placed in a petri dish with an inner diameter of 120 mm containing 60 g of 0.9% physiological saline. It is taken out after 60 minutes, left on a paper towel for 3 seconds, drained, the weight of the apparatus after removing the load is measured, and the absorption capacity under pressure is calculated according to (Equation 5).
(Formula 5) Absorption capacity under pressure of absorbent resin (g / g) = (mass of device after absorption (g) −mass of device before absorption (g)) / (mass of absorbent resin)

In this specification, the water retention ratio of the absorbent resin can be calculated as follows. The tea bag containing the water-absorbing absorbent resin immediately after the Tea-bag method is carried out and placed in a centrifuge, dehydrated at 250 minutes, and the mass is measured. The same operation is performed without using the absorbent resin, the mass is measured to obtain a blank, and the water retention magnification is calculated from these values according to (Equation 6). The measurement is performed three times, and the average value is set as the water retention magnification.
(Equation 6) Water retention ratio of absorbent resin (g / g) = {(mass of tea bag after absorption by centrifugal separator after absorption) − (mass of blank tea bag after absorption) − (mass of absorbent resin) )} /
(Mass of absorbent resin)

  An example of a preferred method for producing the absorbent resin used in the present invention is to polymerize a monomer solution containing an unsaturated carboxylic acid ammonium salt using a radical polymerization initiator and dry the resulting absorbent resin. It is a method to do. This example will be described below.

  The unsaturated carboxylic acid ammonium salt monomer is not particularly limited, and (meth) acrylic acid, itaconic acid, (anhydrous) maleic acid, crotonic acid, fumaric acid, 2- (meth) acryloylethanesulfonic acid, 2- ( Examples thereof include ammonium salts such as (meth) acrylamido-2-methylpropanesulfonic acid, and ammonium salts of (meth) acrylic acid are preferably used. The method for producing the unsaturated carboxylic acid ammonium salt may be a derivative such as a neutralized carboxylic acid, or a hydrolyzate of an unsaturated amide compound or unsaturated nitrile compound produced by a microorganism.

  Other monomers other than the unsaturated carboxylic acid ammonium salt may be added. Other monomer components include methyl (meth) acrylate, ethyl (meth) acrylate, (meth) acrylamide, (meth) acrylonitrile, vinyl acetate, hydroxyethyl (meth) acrylate, methoxyethyl (meth) acrylate, hydroxypropyl (Meth) acrylate etc. are mentioned, Among these, 1 type, or 2 or more types can be added at 50 mol% or less in all the monomer components.

Further, a compound having two or more functional groups that react with an acid group may be added to the absorbent resin. Examples of the compound having two or more functional groups that react with the acid group include ethylene glycol diglycidyl ether, trimethylolpropane triglycidyl ether, (poly) glycerin polyglycidyl ether, diglycerin polyglycidyl ether, propylene glycol diglycidyl ether, etc. Polyhydric alcohols such as (poly) glycerin, (poly) ethylene glycol, propylene glycol, 1,3-propanediol, polyoxyethylene glycol, triethylene glycol, tetraethylene glycol, diethanolamine, triethanolamine Polyvalent amines such as ethylenediamine, diethylenediamine, polyethyleneimine, and hexamethylenediamine;
Also, multivalent ions such as zinc, calcium, magnesium, and aluminum may be added because they react with the acid groups of the absorbent resin and act as a crosslinking agent.

  There is no problem in copolymerizing a polymerizable crosslinking agent which is another crosslinking agent. Examples of polymerizable crosslinking agents include diethylene glycol diacrylate, N, N′-methylenebisacrylamide, polyethylene glycol diacrylate, polypropylene glycol diacrylate, trimethylolpropane diallyl ether, allyl glycidyl ether, pentaerythritol triallyl ether, and pentaerythritol diacrylate mono. Examples include stearate, bisphenol diacrylate, isocyanuric acid diacrylate, tetraallyloxyethane, and diallyloxyacetate. Among these polymerizable crosslinking agents, N, N'-methylenebisacrylamide or trimethylolpropane triacrylate is particularly desirable.

  It is preferable to add a foaming agent as another additive for the purpose of expanding the surface area of the absorbent resin. As the foaming agent, a known carbonate can be used. As the carbonate, any carbonate or bicarbonate including a salt or mixed salt is used in the present invention. Examples of more preferred carbonates for the present invention include sodium carbonate, sodium bicarbonate, potassium bicarbonate, ammonium carbonate, ammonium bicarbonate, magnesium carbonate, calcium carbonate, barium carbonate and the like, and hydrates thereof. One type or two or more types are used. In particular, preferred carbonates for the present invention are monovalent cations such as sodium, potassium, ammonium carbonate or bicarbonate. When a carbonate composed of a polyvalent cation species is used, the polymer having a carboxyl group may be metal-crosslinked by the polyvalent cation species and adversely affect the absorption performance.

  The amount of carbonate added to the monomer aqueous solution is preferably 0.01 to 10% by mass, more preferably 0.1 to 5% by mass with respect to the monomer component. When the amount of carbonate added is less than 0.01% by mass, the hydrogel obtained by polymerization does not become a porous body. Moreover, when it adds exceeding 10 mass%, a water soluble part will increase and it will interfere with the water retention ability of an absorptive resin. Further, it is preferable to add the carbonate before the ultraviolet irradiation. As an addition method, the carbonate may be added as it is, or it may be dissolved in an arbitrary solvent and added as a carbonate solution.

  An antifoaming agent can also be used for the purpose of controlling the foaming agent and the foaming time. As the antifoaming agent, generally known antifoaming agents, antifoaming agents, foam stabilizers and the like can be used, and one kind or a combination of two or more kinds can also be used. Specific antifoaming agents include fats and oils, fatty acids, lower alcohols, superabsorbent alcohols, metal soaps, silicones, hydrophobic silica / silicone compounds, fatty acid esters, polyglycols, poly Examples include glycol esters, polyethers, modified silicones, oil-soluble polymers, organic phosphorus compounds, sulfated fatty acids, polyether derivatives, silica / modified silicone compounds.

  The solvent of the monomer solution is not particularly limited as long as it has excellent monomer solubility. Particularly preferred is water alone, but hydrophilic solvents such as ethanol, methanol and acetone may be used singly or in combination. Moreover, you may add basic compounds, such as salts, such as sodium chloride, and ammonia for the purpose of pH control as needed. As a polymerization method, a known method such as solution polymerization can be used, but aqueous solution polymerization is preferable from the viewpoint of energy, such as not using an organic solvent. The type of the reactor is preferably one that initiates polymerization by heat and / or ultraviolet irradiation, and may be either a batch type or a continuous type. An apparatus such as an endless belt, which is a known reaction apparatus, may be used.

  The polymerization method of the unsaturated monomer is not particularly limited, and generally used methods such as aqueous solution polymerization, reverse phase suspension polymerization, reverse phase emulsion polymerization, spray polymerization, and belt polymerization can be applied. The polymerization initiation method is not particularly limited, and polymerization with a radical polymerization initiator, polymerization by irradiation with radiation, electron beam, or ultraviolet polymerization with a photosensitizer can be performed. Examples of the initiator used for such radical polymerization include persulfates such as potassium persulfate, ammonium persulfate and sodium persulfate; hydrogen peroxide; organics such as cumene hydroperoxide, t-butyl hydroperoxide and peracetic acid. Examples thereof include known initiators such as oxide oxides. When an oxidizing radical polymerization initiator is used, a reducing agent such as L-ascorbic acid or Rongalite may be used in combination.

  As a polymerization initiation method, it is preferable to perform polymerization by irradiating with ultraviolet rays using a radical photopolymerization initiator and a peroxide. Examples of the radical photopolymerization initiator include benzoin, benzyl, acetophenone, benzophenone and derivatives thereof which are generally used for photopolymerization. Examples of derivatives include benzoin-based compounds such as benzoin methyl ether, benzoin ethyl ether, benzoin isopropyl ether, benzoin isobutyl ether, and acetophenone-based compounds such as diethoxyacetophenone, 2,2-dimethoxy-1,2-diphenyl. Ethan-1-one, 1-hydroxycyclohexyl phenyl ketone, 2-methyl-1- (4- (methylthio) phenyl) -2-monfolinopropane-1, 2-benzyl-2-dimethylamino-1- (4- Morpholinophenyl) butanone-1,2-hydroxy-2-methyl-1-phenylpropan-1-one, as benzophenone series, methyl O-benzoylbenzoate, 4-phenylbenzophenone, 4-benzoyl-4′-methyl Diphenyl Rufide, 3,3 ′, 4,4′-tetra (t-butylperoxycarbonyl) benzophenone, 2,4,6-trimethylbenzophenone, 4-benzoyl-N, N-dimethyl-N- [2- (1- Oxy-2-propenyloxy) ethyl] benzenemethananium bromide, (4-benzoylbenzyl) trimethylammonium chloride, 4,4′-dimethylaminobenzophenone, 4,4′-diethylaminobenzophenone, and the like.

  As other radical photopolymerization initiators, azo compounds can be used, and azonitrile compounds, azoamidine compounds, azoamide compounds, alkylazo compounds, and the like can also be used. However, in this case, it is preferable to use a radical photopolymerization initiator having a benzoyl group because it is necessary to add a relatively large amount and it is difficult to increase the degree of polymerization.

  The addition amount of the polymerization initiator is preferably 0.0001 to 0.1% by mass, more preferably 0.001 to 0.01% by mass with respect to the monomer component. When the addition amount of the photopolymerization initiator is less than 0.0001% by mass with respect to the monomer component, the polymerizability becomes extremely low. On the other hand, when it exceeds 0.1% by mass, the low molecular weight tends to increase. Yes, the water-soluble content tends to increase.

  In order to reduce the residual monomer, a known initiator can be used. It is preferable to use a peroxide as the initiator. Examples of preferred peroxides include persulfates such as potassium persulfate, ammonium persulfate, sodium persulfate; hydrogen peroxide; organic peroxides such as cumene hydroperoxide, t-butyl hydroperoxide, peracetic acid, Etc. One type or two or more types can be used in combination. The amount of peroxide added is preferably 0.001 to 10% by mass, more preferably 0.01 to 1% by mass, based on the monomer component. When the amount of peroxide added is less than 0.001% by mass, it is difficult to sufficiently reduce the residual monomer. When the amount added is 10% by mass or more, the water-soluble component increases and the obtained absorbent resin May be colored.

  It is preferable to perform a deoxygenation operation in the monomer solution in advance before the start of polymerization. Specifically, dissolved oxygen is removed by bubbling with an inert gas for a sufficient time. Further, it is desirable that the atmosphere in the reactor is replaced with an inert gas such as nitrogen or helium. In the present invention, the dissolved oxygen in the monomer aqueous solution is preferably 4 ppm or less, more preferably 1 ppm or less. When the dissolved oxygen in the monomer aqueous solution exceeds 4 ppm, the polymerization start time is delayed, the reaction is not completed, and the residual monomer may increase. The inside of the reactor may be any of reduced pressure, normal pressure, and increased pressure.

  From the viewpoint of controlling the polymerization, it is preferable to initiate the polymerization by irradiation with ultraviolet rays. In this case, it is desirable to sufficiently transmit ultraviolet rays into the unsaturated monomer aqueous solution. The thickness of the aqueous monomer solution is preferably 50 mm or less, more preferably 20 mm or less in order to control the reaction temperature (maximum temperature reached by the polymer) and to maintain sufficient UV transmission. When the thickness of the monomer aqueous solution exceeds 50 mm, ultraviolet irradiation is not performed uniformly, and the polymer may become non-uniform. Although there is no restriction | limiting in particular in the lower limit of the thickness of this monomer aqueous solution, When productivity is considered, 1 mm or more is preferable.

  The amount of ultraviolet light is not particularly limited, but is usually preferably 10 to 10,000 mJoul / cm <2>. If the amount is less than this range, polymerization may be insufficient. If the amount is more than this range, excessive crosslinking may result in cleavage of the crosslinking point of the obtained polymer, which may increase the water-soluble content. Moreover, as a light source used for ultraviolet irradiation, a conventionally known light source can be used. For example, a mercury lamp, a metal hydride lamp, or the like may be used in consideration of reaction conditions. The irradiation wavelength is not particularly limited, and light having a wavelength of 200 to 450 nm is usually used. Although the ultraviolet irradiation time is determined so as to be the above light amount, polymerization is started immediately after the irradiation is started under the above conditions, and the polymerization is usually completed in a short time of 10 to 180 seconds.

  The polymerization initiation temperature is preferably 0 to 30 ° C. The unsaturated monomer aqueous solution before the ultraviolet irradiation is preferably maintained at a temperature of 30 ° C. or lower, more preferably 0 to 20 ° C. When the aqueous monomer solution exceeds 30 ° C., the temperature of the reaction system becomes too high, so that the molecular weight may be lowered, the water retention capacity may be lowered, and the water-soluble content may be increased. There is no restriction | limiting in particular about this monomer aqueous solution temperature, What is necessary is just the temperature which this monomer aqueous solution does not freeze, and what is necessary is just 0 degreeC or more normally.

  The concentration of the aqueous monomer solution is not particularly limited as long as the monomer can be dissolved, but is preferably 10 to 70% by mass, and particularly economical when ammonium acrylate is used as the monomer. From the viewpoint of ease of reaction control, 30 to 65% by mass is most preferable.

  When the water-soluble unsaturated monomer starts to polymerize, the temperature in the system rises, but in order to obtain an excellent absorbent resin, it is preferable to keep the maximum temperature in the system at 120 ° C. or less, more preferably Is to keep the temperature below 100 ° C. When the highest temperature in the system exceeds 120 ° C., the water-soluble content of the polymer obtained by polymerizing the monomer aqueous solution may increase. In addition, the water retention capacity may be poor. Various methods can be considered as a method for suppressing the maximum temperature during polymerization, for example, a method of cooling the polymer contact portion from the outside, a method of applying cold air to the polymer, etc., but these methods also increase the equipment, The aforementioned conditions, that is, the monomer aqueous solution concentration is set to 30 to 65%, the temperature of the monomer aqueous solution is set to 30 ° C. or less, and the thickness of the monomer aqueous solution is set to 50 mm or less, preferably 1 to 20 mm. It is desirable to keep the maximum temperature in the system at 120 ° C. or lower by adopting the condition of

  After the reaction, a water-containing gel-like absorbent resin is formed by solution polymerization. It is preferable to dry this after roughly crushing. After drying, it can be pulverized to about several hundred μm. The particle size distribution is desirably within 1 μm to 3000 μm, particularly preferably 301000 μm to 1000 μm, and more preferably 100 to 600 μm. As a method of rough crushing, an apparatus capable of cutting and extruding a rubber-like elastic body can be used. For example, a cutter-type cutting machine, a chopper-type cutting machine, a kneader-type cutting machine, etc. can be used easily. Can be achieved. When a cutter-type cutting machine is used, the polymer is less deteriorated due to the shear during gel cutting. In order to pulverize the dried gel, a conventionally known pulverization method can be employed. For example, it can be pulverized to a desired particle size by a vibration pulverizer, an impact pulverizer, a friction pulverizer, or the like. You may mix a hydrophilic fiber simultaneously at the time of a grinding | pulverization and / or after a grinding | pulverization.

  The drying method is not particularly limited, and vacuum drying and hot air drying are preferable. As the dryer that can be used in the present invention, a normal dryer or a heating furnace can be used, and examples thereof include a hot air dryer, a fluidized bed dryer, an air flow dryer, an infrared dryer, and a dielectric heating dryer. It is done. The drying temperature is preferably in the range of 70 to 180 ° C, particularly preferably 100 to 120 ° C.

  If hydrophilic fibers are mixed before drying, a composite of hydrophilic fibers and absorbent resin can be formed. Mixing may be performed at any time, but mixing after adjusting the particle shape to some extent is preferable because mixing can be performed uniformly. That is, it is preferable that the hydrogel is pulverized, preliminarily dried, pulverized and then mixed. Preliminary drying here refers to a degree of dryness that can be pulverized.

  You may heat-process an absorptive resin after drying. Polymerization can be advanced by the heat treatment, and the degree of polymerization crosslinking can be adjusted. Heating may be continuously performed in the same dryer after completion of heating, or may be a step independent of the drying step. This heat treatment is preferably performed in the presence of hydrophilic fibers.

  The surface strength of the absorbent resin before the heat treatment is preferably 0.1 to 5.5N, more preferably 0.1 to 5N, still more preferably 0.2 to 4N, and Most preferably, it is 2-3N. Such an absorbent resin having a low surface strength is very susceptible to gel blocking and cannot be used in a conventional absorbent structure. However, in the present invention, such an absorptive resin having a low surface strength is preferable because it has a merit in that direct adhesion with hydrophilic fibers becomes strong. When surface strength is too high, adhesiveness with a hydrophilic fiber may fall. Once the absorbent resin and the hydrophilic fiber are bonded, there is almost no influence of the surface strength of the absorbent resin from the viewpoint of adhesive strength. Rather, it is preferable to increase the surface strength of the resin after compounding because the strength of the surface where the absorbent resin and the hydrophilic fiber are in contact with each other increases the adhesive strength or the absorption characteristics.

  By heating the absorbent resin and the hydrophilic fiber in the presence of water, a composite having a large number of directly bonded portions can be formed. It is preferable to directly bond and heat even after reducing moisture to promote cross-linking of the absorbent resin and increase the surface strength.

  At this time, if a compound having two or more functional groups that react with an acid group is present, it acts as a cross-linking agent, increasing the degree of cross-linking of the absorbent resin surface, and obtaining an effect like so-called surface cross-linking. In addition, it is preferable because adhesion to hydrophilic fibers is increased.

  An increase in the degree of crosslinking at the interface with the hydrophilic fiber is preferable because the liquid passing rate from the hydrophilic fiber to the absorbent resin is increased. On the other hand, when the degree of crosslinking inside the absorbent resin is increased, the absorption ratio of the entire absorbent resin may be reduced. In order to prevent this, there are methods such as controlling the time from water addition to drying when producing a composite, and controlling the crosslinking with a heat amount using a crosslinking agent having low reactivity. Controlling cross-linking with the amount of heat means that when heating is performed by heat from outside such as hot air, the external temperature increases compared to the inside of the absorbent resin, and this difference is used to distribute the cross-linking density. is there.

As a method of increasing only the degree of cross-linking of the surface, there is also a method of making the cross-linking agent difficult to penetrate inside by using a mixed solvent of water and an organic solvent when the cross-linking agent is impregnated into the absorbent resin and dispersed. . As the organic solvent used here, alcohol having high affinity with water is preferable.
In addition, since a cross-linking agent having a highly hydrophobic structure or a high molecular weight cross-linking agent is difficult to be absorbed in the absorbent resin, only the surface can be cross-linked even if it is preliminarily contained in the resin. .

  On the other hand, as a method for controlling the crosslinking density, volatile salts such as ammonium salts can be used. That is, since the acid group in the salt state is not condensed and crosslinked, if the acid group before heating is neutralized in advance, the crosslinking does not proceed even in a water-containing state. When salt is volatilized by heating, the salt breaks off from the surface or hydrophilic fibers, so that the cross-linking proceeds only at the portion where the salt has stopped, so increase the degree of crosslinking near the surface or only around the hydrophilic fibers. Can do.

The surface strength is a parameter representing the ease of deformation of the particle surface of the absorbent resin. When the absorbent resin swollen by absorbing liquid at a specific magnification is put in a container and a load is applied, the gel moves and deforms so as to fill the gap of the absorbent resin filled with a gap in the container. I will do it. Since the surface strength is an elastic modulus when the absorbed resin becomes an actual volume, it means the magnitude of interaction between gel particles and the ease of deformation of the surface. A high surface strength indicates that the absorbent resin is difficult to deform. If it is difficult to deform, the absorbent resin and the hydrophilic fiber may be difficult to adhere directly. The surface strength of the absorbent resin of the present invention is determined as follows.
Equipment: Shimadzu Autograph AG-1
Sample: 0.10 g of an absorbent resin was precisely weighed and placed uniformly in the bottom of a cylindrical container having an inner diameter of 20.5 mm and a height of 50 mm, with a nylon sheet having a pore diameter of 75 μm attached to the bottom surface. A 50φ petri dish was prepared, 0.90 g of physiological saline was added, and the cylindrical container containing the absorbent resin was allowed to stand and allowed to absorb and swell for 1 hour.
Measurement: A 1 kN load cell was used, and a cylindrical shaft having a diameter of 19.7 mm was attached. The measurement range is set to 0.2 kN, and is set so that the load cell is lowered at a constant speed of 0.6 mm / min according to the height at which no load is applied to the load cell. The pressure applied to the load cell was recorded over time. Here, the surface strength represents the load (N) when the actual volume is reached. The actual volume of the absorbent resin was calculated using the specific gravity of physiological saline 1.010 g / cm ³ and the specific gravity of the absorbent resin.

  As a condition of the absorbent resin that is easily bonded directly to the hydrophilic fiber, the salt concentration in the vicinity of the surface of the absorbent resin is preferably 50 mol% or more, more preferably 60 mol% or more, and further preferably 70 mol%. The higher the surface salt concentration, the higher the adhesion with hydrophilic fibers. Although there is no restriction | limiting in particular about the surface salt concentration of the absorptive resin in a final absorption sheet, Preferably it is 90 mol% or less, More preferably, it is 80 mol% or less. A lower surface salt concentration of the absorbent resin in the final sheet is advantageous because it is less likely to cause stickiness even when exposed to moist air. In addition, when the particles are brought into contact with each other at the time of swelling after absorbing the liquid, the aqueous solution diffusibility in the composite can be kept high, which is very preferable.

  In order to maintain a high absorption ratio, it is necessary to increase the salt concentration of the entire absorbent resin, but in order to maintain a high liquid diffusibility in the composite, it is desirable to reduce the salt concentration near the surface. It is. That is, it is preferable to increase only the surface salt concentration and increase the internal salt concentration. Specifically, it is preferable to lower the surface salt concentration by 10 mol% or more, more preferably 20 mol% or more, still more preferably 30 mol% or more, compared to the salt concentration at the center of the absorbent resin. is there. The vicinity of the surface means an outer layer portion having a thickness of about 1 μm in the depth direction from the surface.

  The adjustment of the salt concentration in the vicinity of the surface is preferable because it can be performed by heating at the same time as the formation of the direct adhesion with the hydrophilic fiber, so that the adhesive force and the absorbing power can be balanced at a high level. The temperature in this heat treatment is preferably higher by 10 ° C. than the temperature in the drying treatment. The heating condition is composed of two elements, that is, a heating temperature and a heating time, and greatly affects the absorption performance of the absorbent resin and / or the composite. Although it varies depending on required properties, it is preferably higher by 10 ° C or higher than the drying conditions, more preferably 20 ° C or higher, most preferably higher by 30 ° C or higher, and a range of 100 to 250 ° C is preferable. More preferably, it is 115-200 degreeC, More preferably, it is 130-170 degreeC. The heating time is preferably 10 seconds to 5 hours, more preferably 30 seconds to 1 hour, still more preferably 1 minute to 30 minutes. When the temperature is too low, the progress of crosslinking is slow and takes time, and when the temperature is too high, it may be difficult to control the crosslinking. In addition, there is no restriction | limiting in particular about a heat processing apparatus, Well-known apparatuses, such as a hot air dryer, a fluidized bed dryer, and a Nauter type dryer, are used.

In the absorbent sheet, the amount of the absorbent resin is preferably 20 to 300 g / m ^2, more preferably from 50 to 250 g / m ^2, more preferably from 70~200g / m ^2, 90~180g / M ² is most preferred. If the amount is too small, the dry feeling may be inferior. If the amount is too large, the effects such as the absorption rate and the dry feeling are not so changed.

<Method for producing composite>
The composite of the present invention may be produced by any method as long as the absorbent resin and the hydrophilic fiber are directly bonded to each other, but they are in contact with each other in the presence of the hydrophilic fiber, the absorbent resin and water. It is preferable to produce by dehydrating and drying in the state. Thereby, a composite in which the absorbent resin and the hydrophilic fiber are highly bonded is obtained. It is preferable to perform dehydration drying in a state where a compound having a plurality of functional groups that react with the acid group of the absorbent resin is contained as a crosslinking agent.

  In order to make maximum use of the interaction between the absorbent resin and the hydrophilic fiber, it is preferable that the resin is sufficiently mixed before dehydration and drying. In the mixing step, when water is appropriately present at the time of mixing, an appropriate interaction acts between the hydrophilic fiber and the absorbent resin, thereby improving the mixing property.

  When a large amount of water is present in the absorbent resin as a raw material, it becomes difficult to mix uniformly, so the water content of the absorbent resin is 0.1 to 100% by mass with respect to the mass of the absorbent resin. Is preferable (that is, 0.1 to 100 parts by mass with respect to 100 parts by mass of the absorbent resin), more preferably 1 to 40% by mass, and still more preferably 1.5 to 20% by mass. 2 to 12% by mass is most preferable.

  The hydrophilic fiber and / or the absorbent resin may contain water before dehydration and drying. When the absorbent resin is stored in a water-containing state, the absorption performance may be lowered. Therefore, when the absorbent resin is stored as a raw material, it is preferable that the hydrophilic fiber contains water. In this case, if the hydrophilic fibers are stored in humid air, they are naturally hydrated. When the absorbent resin is used immediately, the absorbent resin may contain moisture, and a suitable moisture range can be obtained by using an absorbent resin that is not completely dried after synthesis.

  Mixing with the absorbent resin, the hydrophilic fiber, and water may be performed in any order. When water and the absorbent resin are mixed first, the absorbent resins easily undergo gel blocking, so the hydrophilic fiber and water are mixed, and the mixed state is maintained where the mixed state of the hydrophilic fiber and water is maintained. While mixing the absorbent resin or mixing the absorbent resin and hydrophilic fiber, the water can be added while mixing when the mixed state of the hydrophilic fiber and water is maintained. preferable. In the case of the latter method, it is preferable to use a spray or the like, or to use steam or the like so that water is dispersed as homogeneously as possible. These steps are preferably performed using a Henschel mixer or the like while maintaining the mixed state.

The mass ratio of the absorbent resin to water in the mixture of hydrophilic fiber, absorbent resin and water prior to the dehydrating and drying step is preferably 20: 1 to 1: 5, and is 15: 1-1: 2. More preferably, it is more preferably 10: 1-1: 1, and most preferably 10: 3-10: 7. The amount of water at this time represents the total water content in the absorbent resin and hydrophilic fibers in the water-containing state. When the moisture content before drying is small, the number of locations where the absorbent resin and the hydrophilic fiber are directly bonded tends to decrease, and when too much, the drying time tends to be long.
Since dehydration drying is preferably performed in a state where the hydrophilic fiber and the absorbent resin are in efficient contact, it is preferable to perform drying after the mixing step.

  The dehydration method is not particularly limited, and examples thereof include a method using heating, a method using reduced pressure, and a method using airflow, and a plurality of methods may be combined. From the viewpoint of enhancing direct adhesion between the hydrophilic fiber and the absorbent resin, heating is preferably performed. The method of heating is not particularly limited, and can be freely selected according to the equipment such as a method using hot air, a method using microwaves, a method using infrared rays, and the like. The heating temperature is preferably 60 to 250 ° C, more preferably 80 to 200 ° C, still more preferably 100 to 180 ° C, and most preferably 120 to 150 ° C. When the temperature is low, the drying efficiency tends to deteriorate, and when the temperature is too high, coloring may occur.

  The degree of dehydration is not particularly limited, but the moisture content after drying with respect to the moisture content before drying of the absorbent resin is preferably 70% or less, more preferably 50% or less, and 30% or less. Is more preferable, and most preferably 10% or less.

  The water content after drying is not particularly limited, but is preferably 0.01 to 100% by mass, more preferably 0.1 to 50% by mass, and more preferably 0.5 to The content is more preferably 20% by mass, and most preferably 2 to 10% by mass. If there is too much moisture, the absorption capacity may be reduced.

  In order to efficiently and directly bond the hydrophilic fiber and the absorbent resin, it is preferable that the hydrophilic fiber and the absorbent resin are mixed, then increased to a predetermined moisture content, and then dried. The method for increasing the amount of water is not particularly limited, and examples include a method of immersing in water and a method of spraying water. The water to be hydrated may contain impurities. Examples of the impurities include cations such as sodium ion, ammonium ion and iron ion, anions such as chlorine ion, water-soluble organic compounds such as acetone, alcohols, ethers and amines. For adjusting the pH of the absorbent resin and / or the composite, an acidic or basic one may be used. Considering the contact between the absorbent resin and the base material described later and the absorption capacity, the amount of impurities is preferably at the tap water level, and it is more preferable to use distilled water or ion-exchanged water without impurities alone. .

  A finely agglomerated composite may be obtained after dehydration and drying, and it is preferable to perform a step of loosening this to adjust the particle size. In this step, a mixer or the like used in the mixing step can be used.

  Since the composite can be manufactured by existing equipment (surface crosslinking equipment) of the absorbent resin, it is preferable to manufacture the composite at a place where the absorbent resin is manufactured. In addition, since equipment for producing hydrophilic fibers is owned by sanitary materials companies and paper manufacturers, when making absorbent sheets and absorbent articles for sanitary materials, it is necessary to do so near these places. preferable.

  The composite can be obtained, for example, by dehydrating and drying the hydrophilic fiber and the absorbent resin in contact with each other. Absorbent resins are often obtained as water-containing gels by polymerization. In the case of aqueous solution polymerization, this is roughly crushed, pre-dried, and pulverized to adjust the particle size. At the time of pulverization, water does not completely fly and moisture remains. A composite can be formed by mixing this and hydrophilic fibers, followed by dehydration drying. That is, the composite can be obtained, for example, by a production method including a step of dehydrating the absorbent resin by mixing it with a hydrophilic fiber in a state where the absorbent resin is wet and mixing with hydrophilic fibers. . For example, in the case of suspension polymerization, the gel is dispersed in the solvent after the polymerization, so the hydrophilic fiber is added to the gel and mixed uniformly, and the moisture content is reduced to absorb the hydrophilic fiber. Adhesive resin is preferably adhered. In this case, the water content can be reduced by distillation.

  Fine particles may be formed by pulverization and may be discarded, but it is preferable because the amount of disposal can be reduced by combining with hydrophilic fibers. The mixing of the hydrophilic fibers may be performed by introducing the hydrophilic fibers into a pulverizer. In the case of suspension polymerization, the particle diameter can be adjusted at the time of polymerization. Usually, the water-absorbing absorbent resin is recovered by filtration or centrifugation. Although it may be mixed with the hydrophilic fiber after the collection, it is preferable to introduce the hydrophilic fiber in a state where a solvent is present after the polymerization because uniform mixing is possible.

  In the present invention, the absorbent resin may be crosslinked using a compound having two or more functional groups that react with an acid group. The crosslinking treatment is preferably performed by heating, and the absorbent resin mixed with the hydrophilic fiber can be dehydrated and dried using a surface crosslinking apparatus. When adding a compound with two or more functional groups that react with acid groups, if added before mixing with hydrophilic fibers and dehydrating, compounds with two or more functional groups that react with acid groups with water will absorb. It penetrates to the inside of the resin and a thick cross-linked layer is easily formed, and it is difficult to satisfy the conditions for surface cross-linking. For this reason, it is preferable to add a compound having two or more functional groups that react with an acid group after complexing, and then perform a crosslinking reaction. When a compound having two or more functional groups that react with an acid group is added and when a crosslinking reaction is performed, if a large amount of water is present, the compound diffuses into the interior simultaneously with the diffusion of water. Therefore, the water content in both steps is preferably 20% or less, more preferably 15% or less, and further preferably 10% or less with respect to the weight of the absorbent resin. Preferably, it is most preferably 5% or less.

  A compound having two or more functional groups that react with an acid group is preferably used in an amount of 0.01 to 10 parts, more preferably 0.1 to 5 parts, based on 100 parts by weight of the absorbent resin. Preferably, 0.3-3 parts are used, more preferably 0.5-1.5 parts. If the amount is too large, the absorption capacity may be reduced. Since it is difficult to uniformly spray such a small amount, it is preferable to use an organic solvent. Any organic solvent may be used as long as it can dissolve a compound having two or more functional groups that react with an acid group, and alcohols, ketones, ethers, esters, and the like can be used. Since the organic solvent is preferably recovered and reused, it is preferable to select the organic solvent in consideration of the vapor pressure, the boiling point, and the like. The amount of the organic solvent is not particularly limited, but is preferably 10-10000 parts, more preferably 50-1000 parts, and still more preferably 100-500 parts with respect to 100 parts of the composite weight.

<Absorption sheet>
The composite of the present invention can be formed into a sheet by adhering and fixing to the substrate with an adhesive. Moreover, a sheet | seat can be formed by mixing the composite and thermoplastic fiber of this invention, and a thermoplastic fiber being heat-seal | fused. Normally, when the sheet is formed by these methods, an adhesive component or thermoplastic fiber adheres to the surface of the absorbent resin and inhibits the swelling of the absorbent resin. However, since the composite of the present invention has a sufficient space around the absorbent resin due to the hydrophilic fibers, the probability that these adhesive components directly adhere to the absorbent resin surface is low. For this reason, even when it is made into a sheet, the absorption performance is not impaired, and a thin sheet having a high absorption rate and a dry feeling can be formed. If the composite moves and is biased, the absorption performance may not be stable. Therefore, it is preferable that the composite is substantially fixed to the sheet.

  It is preferable to adjust the performance as an absorbent body by combining the absorbent sheet of the present invention and other sheet-like materials. Depending on the purpose of use of the absorbent sheet, deodorant, fragrance, various inorganic powders, foaming agent, pigment, dye, antibacterial agent, hydrophilic short fiber, plasticizer, adhesive, surfactant, fertilizer, oxidation Agents, reducing agents, chelating agents, antioxidants, heat stabilizers, ultraviolet absorbers, light stabilizers, salts and the like may be contained. In order to increase flexibility, it is preferable to include a surfactant.

  In the present invention, the base material refers to a material that can maintain a sheet shape. In the present invention, the base material may be any material as long as it is a sheet, and examples thereof include paper, cloth, and film. Paper refers to paper in a broad sense defined by JIS P 0001, and cloth is a general term for sheet-like fiber products defined by JIS L 0206. The cloth is classified into a woven fabric, a knitted fabric, a braided article, a lace, a net, and a non-woven fabric according to the means for forming the sheet. The fabric used in the present invention is preferably a woven fabric, a knitted fabric, or a non-woven fabric, and more preferably a non-woven fabric. Paper and cloth are preferable because they are excellent in form stability unlike short fibers such as pulp. Nonwoven fabric is defined by JIS L 0222.

  The raw material for the substrate is not limited, and a plurality of combinations of substrates may be used. If it is a hydrophilic raw material, water permeability can be imparted. If it is a hydrophobic raw material, it can be used as a layer for improving dry feeling on the front side, and as a water-stopping layer on the back side. Can do. The base fiber includes both natural fiber and synthetic fiber, and a combination of a plurality of fibers may be used. The length of the fiber may be short fiber or long fiber. Treatment may be performed for strengthening or imparting hydrophilicity.

  Hydrophilic materials are excellent in liquid absorbency and water permeability, and have a high affinity with hydrophilic fibers and absorbent resins. Hydrophobic ones are excellent in dry feeling and have a characteristic of high affinity with hydrophobic fibers. Since these performances are all preferable as an absorber, it can be said that a base material having both hydrophilic and hydrophobic characteristics is preferable. Having both hydrophilic and hydrophobic characteristics may be a base material in which two or more hydrophilic and hydrophobic materials are mixed, or a hydrophilic material that has been subjected to a hydrophobic treatment, The material may be subjected to a hydrophilic treatment. Further, since the continuous long fiber is superior in liquid permeability to the short fiber, the hydrophilic portion is preferably a continuous long fiber.

The shape of the substrate is not particularly limited, and the thickness is preferably 0.001 mm to 1 cm, more preferably 0.01 mm to 5 mm, still more preferably 0.05 mm to 3 mm, and most preferably 0.1 mm to 1 mm. Mass is preferably ^{0.1g / m 2 ~200g / m 2} , more preferably from ^{0.5g / m 2 ~100g / m 2} , more preferably from ^{1g / m 2 ~60g / m 2} , most preferably ^{2g / m 2 ~30g / m 2} . Those that are too thin or light are not preferred from the standpoint of strength.

  There are hydrophilic and hydrophobic adhesives for bonding the composite to the substrate. Examples of the hydrophilic adhesive include low molecular weight polyvinyl alcohol and carboxymethyl cellulose. As the hydrophobic adhesive, a so-called hot melt adhesive that dissolves mainly by heat is preferably used. Since a hydrophilic adhesive may be dissolved during use to lower the adhesiveness, it is preferable to use a hydrophobic adhesive.

  Any material may be used for the thermoplastic fiber in the present invention, and general polyethylene, polyester, polypropylene, and the like can be suitably used. It can be said that it is preferable to use a fiber having a core-sheath structure in which the amount of fusion can be easily controlled. In this case, it is preferable that the glass transition temperature of the sheath portion is lower than the glass transition temperature of the core portion, or the melting point of the sheath portion is lower than the melting point of the core portion. The difference in melting point between the core and the sheath is preferably 10 ° C. or higher, more preferably 20 ° C. or higher, and further preferably 30 ° C. or higher. One type of thermoplastic fiber may be used, or a plurality of types may be used. It is preferable to use a thermoplastic fiber that exhibits hydrophobicity. In order to adjust the performance, it is also preferable to use fibers that do not exhibit thermoplasticity at the same time, and hydrophilic fibers such as cellulose are appropriately used.

  The thickness of the fiber is not particularly limited, but is preferably 0.01 to 200 denier, more preferably 0.1 to 100 denier, still more preferably 0.5 to 50 denier. Most preferred is 2 to 15 denier. If it is too thin, the space between the hydrophobic fibers may become too small and the absorption performance may be impaired, and if it is too thick, the feel may deteriorate. Although fiber length is not specifically limited, It is preferable that it is 0.1-20 mm, It is more preferable that it is 0.5-10 mm, It is still more preferable that it is 1-5 mm. If it is too short, the bonding force may be weak, and if it is too long, the mixing property may be poor.

The amount of thermoplastic fibers, to the absorbent sheet is preferably 5 to 100 g / m ^2, more preferably from 10 to 80 g / m ^2, more preferably from 15 to 60 g / m ^2,. 20 to Most preferably, it is 40 g / m ² . If the amount is too small, the sheet strength may be weakened. If the amount is too large, the absorption rate may be slow.

  It is preferable that the absorbent sheet of the present invention has a sheet shape and has almost no component to be detached. The absorbent sheet may be separately used in combination with particulates, fibers, etc. In this case, only the part excluding the part that is easily detached is used as the absorbent sheet. The part that is easily detached is the one that is detached from the sheet when it is turned 10 times at a speed of 1 reciprocation per second in the state where the sheet edge is held by hand and the sheet is vertical. Point to.

  The ratio of hydrophilic fibers to hydrophobic fibers in the entire absorbent sheet is preferably 9: 1 to 2: 8, more preferably 8: 2 to 3: 7, and still more preferably 8 in terms of mass ratio. : 2-4: 6, and most preferably 7: 3-5: 5. The more hydrophilic fibers, the higher the liquid trapping power in the sheet, and the higher the hydrophobic fibers, the higher the liquid diffusing power in the sheet. Therefore, it is preferable to adjust these balances.

  The ratio of the absorbent resin to the hydrophilic fiber in the entire absorbent sheet is preferably 10: 1 to 1: 5, more preferably 9: 1 to 1: 3, and 8: 1. More preferably, it is ˜1: 2, and most preferably 8: 2 to 1: 1. The more hydrophilic fibers, the higher the instantaneous water retention, but there is a possibility that the dry feeling is inferior. The more the absorbent resin is, the better the dry feeling is, but there is a possibility that the absorbent resin having a small particle system is not fixed and can be detached.

  When the absorbent sheet is formed by heat-sealing hydrophobic fibers, heating is preferably performed in a state where no load is applied to the sheet. When heating is performed in a state where a load is applied, the space in the sheet is reduced, and the absorption performance may be reduced. As a method of heating in a state where no load is applied, drying with hot air can be given.

  The temperature of the hot air used for drying is preferably 100 to 190 ° C. The optimum temperature differs depending on the melting point of the fiber used, and it is preferable to carry out at a temperature 10 to 60 ° C. higher than the melting point. If the temperature is too low, drying may take too long, and if the temperature is too high, it becomes difficult to control the amount of melting. As a wind speed, 0.1-100 m / s is preferable, It is more preferable that it is 1-40 m / s, It is still more preferable that it is 3-20 m / s. Preferable apparatuses used for hot air drying include various hot air dryers such as a batch type hot air dryer and a conveyor type hot air dryer.

  In order to make the temperature inside the sheet uniform during heating, it is preferable to heat the sheet with moisture. When water is present, the temperature in the system is maintained at 100 degrees until the water evaporates, and thus the water is heated uniformly. In addition, moisture has a high affinity with hydrophilic fibers and absorbent resins and has a low affinity with thermoplastic fibers, so a repulsive force is generated and an appropriate space is easily secured.

  When heating is performed at the time of sheet molding, a crosslinking reaction with a compound having a plurality of functional groups that react with acid groups can be advanced by this heating. In this case, the composite as the sheet raw material is not surface-layer crosslinked, but there is no problem because the composite in the sheet is surface-layer crosslinked.

  The absorbent sheet of the present invention is, for example, started by dropping when the absorbent sheet is cut into a rectangle of 160 mm length and 70 mm width, placed on a table, and 15 g of physiological saline is dropped over 1.5 seconds. The time (absorption rate (second)) from when the liquid is absorbed and the liquid on the surface of the absorbent sheet becomes invisible is preferably 13 seconds or less, and more preferably 10 seconds or less. Also, for example, after 5 minutes from the start of dropping, a square filter paper having a length of 100 mm and a width of 100 mm, which has been measured in advance, is placed on the dropping position, and 3.5 kg of the same bottom area as the filter paper is placed thereon. The weight increase (rewetting amount (g)) when the weight is applied, the weight is removed 3 minutes after the filter paper is placed, and the weight of the filter paper is measured is preferably 0.2 g or less. More preferably, it is 1 g or less.

<Absorbent article>
The absorbent sheet of the present invention can be made into an absorbent article as it is by adding auxiliary members such as a water-permeable sheet, a water-impermeable sheet, and a gather as needed. Since this absorbent article is thin and excellent in absorption speed and dry feeling, it can be suitably used for disposable sanitary materials such as disposable diapers, urine pads, and sanitary napkins.

  In the manufacturing method of the absorbent article of the present invention, it is preferable from the viewpoint of productivity that the manufacturing process of the absorbent sheet and the auxiliary member mounting process are performed on the same line. Since the absorbent sheet in the present invention has high productivity, it has a sufficient production speed as a sanitary material. In addition, when the absorbent sheet of the present invention is used as a sanitary material, it is thin and has sufficient absorption capacity, so the number of sanitary material use members can be reduced. For this reason, the number of machines can be reduced and productivity can be improved as compared with the conventional sanitary material process.

  Moreover, the absorbent sheet of this invention can obtain an absorbent article with a good fit by combining with an elastic nonwoven fabric. When a conventional absorbent body is combined with such a stretchable nonwoven fabric, the absorbent performance is lowered during stretching, but the absorbent sheet of the present invention is preferable because it can exhibit the absorbent performance in any situation.

(Elastic nonwoven fabric)
The stretchable nonwoven fabric in the present invention is not particularly limited as long as it is a stretchable material, and may be anything. The stretchable nonwoven fabric used in the present invention is composed of stretchable composite fibers. For example, an elastic composite fiber having a high degree of elasticity, a high volume feeling, and a good touch can be efficiently obtained by the following method.

  A stretchable fiber and a non-stretchable fiber each made of an incompatible elastic polymer and a non-elastic polymer are integrated to form a composite fiber in which the stretchable fiber and the non-stretchable fiber are alternately exposed in the circumferential direction. When the ratio of each exposed portion of the stretchable fiber extending in the length direction on the surface of the composite fiber is determined using the maximum exposed portion surface area as the denominator and the surface area of the other exposed portion as the numerator, each value is 0. To satisfy less than 8. A method for calculating the surface area of the exposed portion will be described later.

  By stretching this composite fiber in the length direction, the stretchable fiber and the non-stretchable fiber are separated, the non-stretchable fiber is crimped in three dimensions, and the nonstretchable fiber is entangled in a spiral shape with the stretchable fiber. To form a stretchable conjugate fiber. In addition, when there is only one exposed portion made of stretchable fiber, the exposed portion is regarded as the maximum exposed portion, and the surface area per unit fiber length of the other exposed portions is considered to be 0, and the above ratio is Satisfy less than 0.8. In this way, since the surface area of each exposed portion is different, the stress that contracts when the composite fiber is stretched differs between these exposed portions. Therefore, the magnitude of the shear stress acting on the boundary surface between the stretchable fiber and the non-stretchable fiber is also different. Therefore, the non-stretchable fiber is distorted, and the stretchable fiber and the nonstretchable fiber are easily separated by this strain. Become. Since the separation is almost complete in this way, the degree of stretch of the composite fiber is improved.

  When the ratio of the surface area of the maximum exposed portion to the surface area of each other exposed portion (the size is 0 when there is no other exposed portion), it is less than 0.8, preferably 0. By forming so as to satisfy less than 5, the magnitude of the shrinkage stress is greatly different between the maximum exposed portion and the other exposed portions, the displacement stress becomes large, and the separation efficiency is particularly good. Since the separation efficiency is good in this way, the fineness of the composite fiber can be made smaller than before, and can be made thinner and smoother. In addition, since the distortion causes a large three-dimensional crimp in the non-stretchable fiber after separation, the composite fiber becomes bulky and the volume feeling is increased.

  The three-dimensional crimped non-stretchable fibers are spirally entangled with the stretchable fibers, and the ratio of the non-stretchable fibers surrounding the stretchable fibers increases, so that the touch is improved. Thus, since it can isolate | separate enough only by extending | stretching, the composite fiber which has a stretching property can be manufactured efficiently, and manufacturing cost can be restrained comparatively cheaply.

  Such a composite fiber may be stretched and then mixed with other fibers or twisted alone to form a stretchable yarn, or mixed with other fibers or formed into a nonwoven fabric alone and then stretched to form a stretchable nonwoven fabric. Also good.

  In 100% by mass of the elastic conjugate fiber, it is preferable that the proportion of the elastic fiber is 30 to 90% by mass because both the spiral entanglement and the touch are improved. More preferably, it is 40-80 mass%. When the proportion of the stretchable fiber is too small, the shrinking stress becomes too small and separation becomes difficult, and the nonstretchable fiber is not easily entangled with the stretchable fiber. On the other hand, if the proportion of the stretchable fiber is too large, it becomes difficult to eliminate the rubber-like feel of the elastic polymer.

  When this elastic composite fiber contains at least one of a hydrophilic component, an antibacterial component, and a deodorizing component, it has a specific function according to the contained component, that is, a hydrophilic function, an antibacterial function, and a deodorizing function. Can do.

  When a composite fiber is formed from the stretchable fiber and the non-stretchable fiber by the above-described method and then stretched, the stretchable composite fiber in which the non-stretchable fiber is entangled in a spiral shape can be efficiently produced. . This stretchable composite fiber is bulky and has a good touch and appearance.

  Hereinafter, it will be described in detail with reference to the drawings. The stretchable nonwoven fabric 1 according to the embodiment shown in FIG. 1 is manufactured from a raw material A made of an elastic polymer and a raw material B made of an inelastic polymer. The raw material A and the raw material B are preferably thermoplastic polymers. Here, the raw material A and the raw material B are selected to be incompatible with each other.

  As the raw material A, urethane-based, styrene-based, ester-based, ethylene-based, vinyl chloride-based, nylon-based and other elastic thermoplastic polymers are suitable, and mixtures thereof may be used, and these elastic thermoplastic polymers are mainly used. If so, a non-elastic thermoplastic polymer may be contained by several%. As the raw material B, non-elastic thermoplastic polymers such as polyester-based, polyolefin-based, nylon-based, and polyvinyl alcohol are suitable, and a mixture thereof may be used. If these non-elastic thermoplastic polymers are mainly used, elastic Several percent of the thermoplastic polymer may be contained.

  These raw materials A and B may be kneaded with hydrophilic components, antibacterial components, deodorant components, and the like. As the hydrophilic component, various water-soluble polymers such as various stearates, various sodium sulfonates, and polyethylene oxide are considered. These are about 0.2 to 7% by mass in one of the raw materials A and B, or the raw materials A and B. It is good to mix about 0.2-14 mass% in both. Examples of the antibacterial component and deodorant component include titanium oxide, white carbon, silver compound, zeolite, bamboo extract, etc., and these are about 0.2 to 2.0% by mass in one of raw materials A and B, or About 0.2 to 2.0 mass% may be mixed in both raw materials A and B.

  In order to manufacture the stretchable nonwoven fabric 1 from the raw materials A and B, a process as shown in FIG. 2 is performed. As shown in the figure, first, the raw materials A and B are respectively charged into the hoppers 21 and 22, heated and melted by the extruders 23 and 24, and supplied to the die 25. A passage extending in the vertical direction is formed inside the die 25, and the raw materials A and B circulate therethrough. In addition, a plurality of substantially circular minute nozzle openings 25 a communicating with the passage are formed in parallel on the lower surface of the die 25 in the vertical and horizontal directions.

  Here, the nozzle opening 25a has a shape as shown in FIGS. 3A, 3B, and 3C. That is, in the case of FIG. 3A, it is composed of a substantially bee-shaped central opening 25b and a substantially elliptical side opening 25c pointed in the major axis direction adjacent to both sides thereof. In the case of FIG. 3 (b), a deformed square central opening 25b composed of three sides having a concave arc shape on one side and one side having a convex arc shape, and three concave arc-shaped sides of the central opening 25b, respectively. It consists of a substantially elliptical side opening 25c pointed in the adjacent major axis direction. Further, in the case of FIG. 3 (c), it consists of a substantially ginkgo leaf-shaped central opening 25b and a substantially double-leaf-shaped side opening 25c adjacent to the lower side thereof.

  The raw material A melted from the extruder 23 is supplied to the central opening 25b, and the raw material B melted from the extruder 24 is supplied to the side opening 25c. Thus, the stretchable elastic fiber 11 made of an elastic thermoplastic polymer is spun from the central opening 25b, and the non-stretchable non-stretchable fiber 12 made of an inelastic thermoplastic polymer is spun from the side opening 25c. And are integrated in the molten state at the same time as spinning. In this integrated state, since the raw material A and the raw material B are incompatible with each other as described above, they do not melt or mix. Therefore, corresponding to the shape of the nozzle opening 25a of the die 25, the stretchable fiber 11 and the non-stretchable fiber 12 as shown in FIGS. 4A, 4B, and 4C are alternately exposed on the surface. A composite fiber 10 is formed. Here, the exposed portions where the stretchable fibers 11 are exposed on the surface of the composite fiber 10 are two of 11a and 11c in the case of FIG. 4A, and in 11B, 11d and 11e in the case of FIG. 4B. There are three, and in the case of FIG. 4C, it is one of 11f.

  The raw material ratio and the like of the composite fiber 10 are appropriately adjusted so that 30 to 90% by mass of the elastic fiber 11 is 100% by mass. Moreover, as can be seen from FIGS. 4A, 4 </ b> B, and 4 </ b> C, the maximum exposed portion having the maximum surface area among the plurality of exposed portions 11 a to 11 e exposed on the surface of the composite fiber 10 of the stretchable fiber 11. The ratio of the sizes of 11a and 11b and the surface areas of the other exposed portions 11c, 11d, and 11e, that is, the ratio of the circumferential length in the cross section of the composite fiber 10 has the following relationship. That is, when the size of the surface area per unit length is represented by S (11a) to S (11e), S (11c) / S (11a) <0.8, S (11d) / S (11b) <0.8 and S (11e) / S (11b) <0.8 are satisfied. Further, in the case of FIG. 4C in which there is only one exposed portion 11f, the surface area of the other exposed portions is 0, and if the exposed portion 11f is considered to be the maximum exposed portion, 0 / S (11f) is also obtained. = 0 <0.8 is satisfied.

  As shown in FIG. 2, the composite fiber 10 passes through a cooling chamber 26 disposed below the die 25. A cooling blower 27 is connected to the cooling chamber 26, and air is constantly sent into the room. Therefore, the composite fiber 10 passing through here is cooled while being stretched by air.

  As shown in FIG. 2, a collection conveyor 28 is disposed below the cooling chamber 26. The collection conveyor 28 includes a pulley 28a and a net-like endless belt 28b that is rotationally driven by the pulley 28a. The collection conveyor 28 has a suction box 29 built therein. A suction blower 30 is connected to the suction box 29. Therefore, a suction force is applied to the net-like endless belt 28 b by the suction box 29. Thus, the composite fiber 10 passing through the cooling chamber 26 is collected and collected by being sucked onto the collection conveyor 28 to become a fiber web, and is sent out toward the discharge end of the collection conveyor 28 by the rotation of the endless belt 28b. It is.

  The fiber web discharged from the discharge end of the collection conveyor 28 is guided by the guide roller 31 and sent to the pair of hot embossing rollers 32. The fiber web is sandwiched between hot embossing rollers 32 and point bonded to form a fiber sheet.

  This fiber sheet is further fed into two pairs of nip rollers 33. The fiber sheet between the nip rollers 33 is opened after being given a certain elongation, preferably 70% or more.

  At the time of elongation, due to the above-described surface area relationship, a large shear stress is generated at the boundary surface between the stretchable fiber 11 and the non-stretchable fiber 12, so that they are smoothly separated. Further, as shown in FIG. 5, the three-dimensional crimp is generated in the non-stretchable fiber 12, and this is entangled with the stretchable fiber 11 in a spiral shape. In this way, the stretchable nonwoven fabric 1 is obtained which is bulky and rich in volume, has a high degree of stretch, and has a good feel with no rubber-like feel. This stretchable nonwoven fabric 1 is once wound around a winder roller 34 and then cut for use.

  In this embodiment, the stretchable nonwoven fabric 1 is formed from the composite fiber 10, but the composite fiber 10 similarly formed by melt spinning is directly stretched in the length direction by feeding it directly into two pairs of nip rollers. The stretchable fiber 11 and the non-stretchable fiber 12 may be separated to form a stretchable composite fiber. A stretchable yarn can be obtained by mixing such a stretchable composite fiber with another fiber or twisting it alone. Furthermore, this can be woven with a loom to form a stretchable woven fabric.

  In the embodiment, the cross-sectional shape of the conjugate fiber 10 is circular. However, the shape is not limited to this, and may be a polygonal shape or a hollow donut shape, for example. Further, the structure composed of the stretchable fiber 11 and the non-stretchable fiber 12 of the composite fiber 10 is not limited to the embodiment as long as the above-described surface area relationship or mass ratio relationship is satisfied. Can be changed.

<Production apparatus for composite and absorbent sheet>
Next, although the preferable example of the manufacturing apparatus of the composite of this invention and an absorption sheet is demonstrated, the manufacturing apparatus of the absorption sheet of this invention is not limited to the following.

(A) Apparatus for pulverizing hydrophilic fibers When the hydrophilic fibers are in a sheet or roll shape, the average particle diameter can be adjusted by pulverization. A general pulp sheet crusher can be suitably used. The ground hydrophilic fiber can be stored in a normal tank.

(B) A device for mixing hydrophilic fibers and absorbent resin A device for weighing hydrophilic fibers stored in a tank and an absorbent resin stored in another tank in an arbitrary ratio. It is preferable to have. A general mass meter can be used for measuring the mixing ratio. For mixing the weighed hydrophilic fiber and the absorbent resin, it is preferable to use a container capable of airflow mixing, for example, a hopper having a spiral groove formed therein. The mixture deposited in the lower part can be sent to the next step by controlling the number of revolutions using, for example, a screw.

(C) Apparatus for increasing water content When the water content of the absorbent resin is small, it is preferable to increase the water content. In order to uniformly contain water, it is preferable to increase the water content while mixing the hydrophilic fiber and the absorbent resin with a mixer or the like. As a device for increasing the moisture content, a water spraying device can be suitably used. As the water spraying device, for example, a spray can be used. (B) and (c) may use the same apparatus. While mixing the hydrophilic fiber and water, the absorbent resin may be fed thereto.

(D) Apparatus for dehydrating and drying A hot air dryer can be suitably used for dehydrating and drying. This dryer may be installed on the aforementioned conveyor, or may be a stationary dryer. When drying time becomes long, a stationary dryer is preferable. The dried composite can be stored in a tank or the like.

(E) Apparatus for mixing the composite and a compound having two or more functional groups that react with acid groups The same apparatus as in the above step (b) can be preferably used. It is preferable that the apparatus can perform heating. On the other hand, since it is possible to heat the sheet, it is not always necessary to perform the heating here.

(F) Apparatus for mixing composite and hydrophobic fiber The same apparatus as in step (b) above can be suitably used, but an air stream can be flowed in order to use the mixed material for the sheet forming process. It preferably has a structure. By controlling the air flow rate, a fixed amount can be supplied to the sheet forming process.

(G) Sheet forming apparatus Sheet forming can be performed by, for example, a conveyor system, and a metal net conveyor having good thermal conductivity can be preferably used. In order to make the thickness of the raw material supplied to the conveyor uniform, it is preferable to have a device for sucking from the lower part of the net. In the case of using a sheet, it is preferable to also have a sheet feeding section. Moreover, you may have the apparatus which supplies a hydrophobic fiber, a hydrophilic fiber, and an absorptive resin uniformly. After all the raw materials have been supplied, it is preferable to press in order to make the thickness uniform. For example, a roller press can be suitably used as the press, and the surface of the roller press may be embossed. In order to increase the efficiency of the subsequent heating process, the temperature of the press may be increased. The apparatus for melting the hydrophobic fiber into a sheet by heating can use a normal hot air dryer, and can be formed by heating continuously. A tunnel drying method in which the conveyor passes through the dryer may be used, or a drum method may be used. It is preferable to have a press device in order to make the thickness uniform after heating. When the molded sheet is used as a product as it is, it can be wound up on a winding device. You may provide the slit apparatus for aligning a width | variety. In the case where the hydrophilic fiber and / or the absorbent resin and / or the hydrophobic fiber are not mixed in advance, the respective raw materials can be directly supplied onto the conveyor and formed into a sheet by the same operation.
(F) An absorption sheet can also be formed using an adhesive for the substrate without performing the step. In this case, an absorbent sheet can be produced if there is a substrate feeding device, a device for applying an adhesive to the substrate, and a device for quantitatively feeding a composite.

(H) Absorbent article manufacturing apparatus (g) The absorbent sheet molded in the step can be taken up as it is and sent directly to a general absorbent article manufacturing step. For example, if there is a device that feeds a water-permeable sheet called a so-called top sheet, a device that sends out a waterproof sheet called a so-called back sheet, and an adhesive device, an absorbent article can be produced as it is. The process of the article can be greatly simplified. Of course, it is also possible to provide a gathering device, a tape attaching device, and a die-cutting device that are used in general absorbent article manufacturing.

  In this invention, the manufacturing apparatus of an absorbent article is not specifically limited, The apparatus used for manufacture of the conventional absorption sheet can be used. Specifically, the absorbent sheet according to the present invention is supplied onto the continuous body of the backsheet material located on the peripheral surface of the work drum while conveying the continuous body of the backsheet material along the peripheral surface of the work drum. After fixing, the continuous body of the backsheet material is cut to a length corresponding to the size of the absorbent article. In the absorbent article of the present invention, it is preferable to provide a top sheet, and before cutting the continuous body of the backsheet material into a length corresponding to the size of the absorbent article, the continuous body of the topsheet material is removed from the work drum. It can manufacture by adhering to the continuous body of the raw material for back sheets, and an absorption sheet.

<Method for producing absorbent article>
It is preferable that the absorbent article which concerns on this invention is comprised from the absorption sheet and auxiliary member of this invention, or the absorption sheet of this invention, and an elastic nonwoven fabric. Examples of the auxiliary member include a top sheet provided on one surface of the absorbent sheet, a back sheet provided on the other surface of the absorbent sheet, a water-permeable sheet, a water-impermeable sheet, and a gather.

An absorptive article can be manufactured with a manufacturing method provided with the process of pasting up the absorption sheet of the present invention, the top sheet sent out continuously, and / or the back sheet sent out continuously, for example.
Further, the manufacturing method of the absorbent article includes a step of supplying and fixing the absorbent sheet onto the continuous body of the backsheet material conveyed along the peripheral surface of the work drum, and a backsheet to which the absorbent sheet is fixed And a step of cutting the continuous material for use into a length corresponding to the dimension of the absorbent article.

In this case, before the step of cutting the continuous body to which the absorbent sheet and the backsheet are fixed, the continuous body of the topsheet material is supplied and fixed to the continuous body of the backsheet material to which the absorbent sheet is fixed. A process can be further provided.
Moreover, it is preferable from a viewpoint of productivity that the manufacturing process of the absorbent sheet of the present invention and the process of wearing the auxiliary member in manufacturing the absorbent article are on the same line.

<Application of absorbent sheet>
The absorbent sheet of the present invention is an absorbent member for disposable sanitary materials such as disposable diapers, urine pads and sanitary napkins, an absorbent member for excrement disposal materials for pets such as animal sheets and pet sheets, and transport of frozen marine products. Absorbent sheet to prevent marine products from getting wet with iced water, or absorbent sheet for preventing water evaporation covering potted plant, absorbent sheet laid under potted plant, absorbency placed around aquarium Absorbent sheets used for seats, sheets for anti-condensation materials, etc., water drop absorption mats that are placed in dripping places such as receiving parts of umbrella stands, etc. to absorb water drops falling from umbrellas, etc., as mats for vehicle head covers Or a toilet paper sheet after defecation in a mat for preventing dampness in a helmet or hat, for example, a warm water-washed toilet seat (such as a Washlet (registered trademark) toilet bowl made by TOTO Corporation) Absorbent mats to prevent floor wetness due to rain on rainy days in event venues without roofs in rainy weather, absorbent mats to prevent wet floors of vehicles such as cars, trains or airplanes on rainy days, Absorptive mats for preventing wetness of floors of hospitals, service areas, department stores, hotels, stores, office buildings or leisure facilities, absorbent mats for preventing wettability in refrigerators, absorbent mats for preventing wetness of floors of kitchens, Absorption sheet for drip absorption of kitchen garbage or kitchen garbage, water supply equipment, hot water supply equipment or hygienic appliances such as toilets or toilets, floor wetting prevention absorbent mats, and floor wetting around the refrigerator Absorbent mats for prevention, sheets for leisure mats or massage therapy, and auxiliary mats for beds, packaging with water retention or humidity control functions for vegetables, fruits and vegetables Packaging materials with water retention or humidity control functions such as food, fresh fish, raw meat, prepared foods or lunch boxes, as well as packaging materials for seeds, strains, seedlings or bulbs, cleaning machinery and windows, ceilings and walls of buildings Further, it can be preferably used as a waste cloth or a cloth for wiping off dew condensation and wetting on the floor or window, etc., for preventing water evaporation during cultivation of horticultural plants.
In particular, since it has excellent absorption speed and dry feeling, it can be suitably used for absorbent members of disposable sanitary materials such as disposable diapers, urine pads, and sanitary napkins.

  The absorbent sheet of the present invention is suitable as an absorbent sheet for a grill pan. The grill in the present invention refers to a cooking utensil for a roasting cooking method. Heat radiation is the main heating source for roasting, in addition to direct fire, by electromagnetic waves, by heating metal plates and far-infrared ceramics to high temperatures by gas combustion, and using infrared radiation emitted from this for cooking, What uses the Joule heat of an electric heater as a heat source may be used.

  An example of the grill is a grilled fish. Normally, it is a mechanism that is built into a gas stove and burns fish. What to bake is not limited to fish. The grilled fish has a small internal volume compared to the so-called grills and ovens, but can cook all grilled dishes that are not so large per dish. For example, grilled fish (from grilled fish such as gratin, hashed potatoes and pizza) Can handle a wide range of Japanese dishes such as sword fish and dried fish. However, if the oil attached to the inside is not cleaned and the grill pan is not filled with water, it may ignite and burn, causing problems.

  Even when water is used, there is a problem that if the oil falls directly on the water, the oil scatters and it takes a lot of trouble to clean the oil. If the absorbent sheet of the present invention is used while being spread on a grill pan, the grill pan will not become dirty because the absorbent sheet absorbs oil. Although it is difficult for normal absorbent resin to absorb oil, in the structure of the absorbent sheet of the present invention, it is possible to absorb oil because it has voids inside the sheet. Moreover, oil can be confined in the hydrophobic part in a sheet structure by making a hydrophobic fiber exist or using a hydrophobic base material.

  When oil is held inside, there is a merit that the amount of odor generated decreases. When cooking with a lot of oil, a method of using a large amount of water and placing the absorbent sheet of the present invention on it is also possible. In this case, since the absorbent sheet floats on water, it becomes easy to absorb oil. The absorbent sheet of the present invention can be easily removed because the absorbent sheet after use can be prevented from being deformed.

  When there is detachment of the absorbent resin, it becomes difficult to wash, but the absorbent sheet of the present invention does not detach the absorbent resin, so it is easy to wash the grill. Furthermore, there is an effect that the smell generated by baking is also adsorbed, and there is an advantage that it is not necessary to worry about the smell of the room without turning on the ventilation fan. Furthermore, the absorbent sheet of the present invention can be used multiple times. You can remove it and clean the grill, then leave the same sheet, or you can use it without washing.

  When removing, you may dry and preserve | save. If you use it as it is without washing, you may forget to pour water, but the grill usually has a sealed structure, and the moisture absorbed by the absorbent resin is not easily separated. If the sheet shape collapses, there may be separated fibers and the like, and the portion may be burned and odors may adhere to the food, but the structure of the absorbent sheet of the present invention is maintained. This problem does not occur.

  In the conventional sheet where the absorbent resin falls off after absorption, it becomes cumbersome rather than easy to clean after use, and if the absorbent resin adheres to food, it will be delicious because it will drain the moisture of the food It is impossible to use multiple times. There is also an example in which a conventional absorbent sheet is installed on the absorbent tray (for example, Japanese Patent Application Laid-Open No. 2005-124833), and it is said that the tray can be disposed of. However, the tray is not only wasteful and increases dust, but also a grill because it is bulky Some types cannot be used. Furthermore, the absorbent resin may be detached and spilled. This type is difficult to reuse because its performance changes once used.

  The absorbent sheet of the present invention can be suitably used as a bag absorbent sheet. The cocoon is used to keep the body, and may be for humans or animals. Currently, when corpses are kept (whether humans or animals) (棺 桶), “dry ice” is placed on the side or under the corpse regardless of summer or winter (summer season, June to August). Absorption of secretions from the corpse And use absorbent sheets to prevent (delay) rot. The absorbent sheet of the present invention is superior in the use efficiency of the sheet because the liquid diffusivity is excellent compared with the conventional absorbent sheet, and the liquid and odor are uniformly absorbed by the entire surface of the sheet.

  Further, in the conventional absorbent sheet, the absorbent portion is raised and the body remains dirty and the appearance is deteriorated, but this is not the case with the absorbent sheet of the present invention. Furthermore, the absorbent sheet of the present invention is a suitable sheet that can achieve its original purpose with a small amount of resources.

  The absorbent sheet of the present invention can be suitably used as an absorbent sheet for anti-condensation material. By adhering the absorbent sheet of the present invention to a window or the like, it is possible to quickly and surely absorb the condensed water generated on the surface of the building such as the glass surface, window frame, wall surface, etc. Can be avoided. There are various absorption sheets for anti-condensation materials, such as those using the hygroscopicity of acidic paper, those incorporating silica gel powder on neutral paper, and using single silica gel. There is a limit to the amount of moisture absorbed.

  The absorbent sheet of the present invention is characterized by a large absolute absorption amount (several times or more than silica gel) of the absorbent resin. Moreover, even if excessive moisture is sucked, it does not become a solution. Furthermore, since there is little rewet, water does not spill during contact. By blending each material in a well-balanced manner, it is flexible and thin, and can be easily cut and pasted at a place where it is desired to be installed, and is suitable for an absorption sheet for a dew condensation prevention material.

  If moisture is absorbed only with a conventional general absorbent resin sheet, the absorbent resin may swell and become sloppy and fall off, so if the absorbent resin sheet is not covered with a bag-like material such as a nonwoven fabric As a result, there are disadvantages that the thickness is increased and the production equipment and raw material costs are high. In addition, after being attached to the glass surface, it is usual to regenerate the absorption capacity by evaporating the absorbed water by natural drying without peeling off over a long period of time. The conventional absorbent resin sheet absorbs a large amount specifically at the place where condensed water touches, and the overflowed liquid diffuses after reaching saturation. For this reason, there is a problem that the overflowed material is likely to leak, and there is a problem that it is difficult to regenerate the absorption capacity because the surface area of the absorbent resin that has absorbed the liquid is small. For this reason, especially when the amount of condensed water generated on the glass surface is large and the amount of condensed water exceeds the absorption capacity of the absorbent sheet for anti-condensation material before its absorption capacity is regenerated, the condensed water will fall. There was a problem of collecting in the frame.

  The absorbent sheet of the present invention has the advantage that it can be uniformly absorbed as a whole, so that it does not easily overflow, and the entire absorbent resin is used for absorption, so the surface area is large and the absorption capacity is regenerated by transpiration. There is a merit that it is easy to do.

  The absorbent sheet of the present invention can be suitably used as an absorbent sheet for a sweat pad. By arranging the absorbent sheet of the present invention on the side, forehead, neck, back, etc. as a sweat pad, it is possible to absorb sweat and keep it clean. What is required for a sweat pad is an absorption speed, a dry feeling, and a wearing feeling. There are sweat-absorbing pads for the purpose of absorption speed and dry feeling, but none that take into account the feeling of wearing after absorption.

  Since the absorbent sheet of the present invention can be absorbed uniformly as a whole, there is an advantage that the fit does not change before and after the absorption of sweat. Furthermore, since the absorbent sheet of the present invention is excellent in flexibility, it is excellent in wearing feeling. Naturally, since there is no detachment of the absorbent resin, there is no problem that the absorbent resin touches the body and feels bad. The absorbent sheet of the present invention has a sufficient absorption rate because the hydrophilic fibers quickly take sweat into the structure of the absorbent sheet, and is excellent in dry feeling because the liquid is sent from the hydrophilic fibers to the absorbent resin.

  Absorbing ammonia also has the effect of preventing odors. In addition, typical production methods such as conventional sweat pads are mainly produced by applying or remodeling equipment for preventing dripping of breast milk (breast milk pads) for armpits. Large and poor production efficiency (slow speed). Conventional equipment includes (1) film process, (2) undersheet supply, (3) pulverization process, (4) absorbent resin spreading process, (5) folding process (2-3 folds), (6) nonwoven fabric winding process , (7) Sealing and punching process, (8) Counting, (9) Alignment, which is very complicated and has low production efficiency and high cost. The conventional product for the purpose of removing sweat pads (sheets) requires a separate production machine, except for the sanitary napkin production machine and the width (for forehead, neck, back, etc.). It's expensive.

  The absorbent sheet of the present invention can be obtained by simply applying a sheet (laminated on one side of the sheet if a waterproof body is required) to a winding machine in the form of a take-up roll and slitting or punching it into an arbitrary shape. Can be made easily, so material costs are low, production costs are low, productivity is high, and sweat-related products that are superior to conventional products can be made.

  The absorbent sheet of the present invention can be suitably used as an absorbent sheet for clothes antifouling pads. The absorbent sheet for clothes antifouling pad is a sheet for preventing the clothes from being soiled by being attached to a particularly easily contaminated collar or sleeve. This is especially effective for white shirts. Clothes stains occur when sebum stains oxidize with increasing temperature. Since sebum dirt is discharged from the skin together with sweat, it is possible to prevent clothes from being stained by absorbing it simultaneously with sweat. The absorbent sheet of the present invention is excellent in antifouling effect because it easily absorbs sweat and oil is easily taken into the absorbent sheet. Furthermore, it is characterized by being soft and excellent in wearing feeling and excellent in fitting feeling even when sweat is absorbed. When the absorbent resin is desorbed, the feel becomes worse but the problem does not occur. Absorbs ammonia and exerts odor prevention effect.

  The absorbent sheet of the present invention can be suitably used as an absorbent sheet for bedding covers. Bedding refers to pillows, mattresses, comforters, beds, and sheets. When sleeping, a large amount of sweat is generated, and sebum dirt is discharged at the same time. By absorbing sebum dirt and sweat at the same time, it is possible to prevent the bedding from becoming dirty. The absorbent sheet of the present invention is excellent in antifouling effect because it easily absorbs sweat and oil is easily taken into the absorbent sheet. Furthermore, it is soft and has a good touch, and even when it absorbs sweat, the touch does not deteriorate. When the absorbent resin is detached, not only the feeling is deteriorated but also a cleaning problem occurs, but the problem does not occur. Absorbs ammonia and exerts odor prevention effect.

  The absorbent sheet of the present invention can be suitably used around food. For example, as an absorbent sheet for a thawing pad when thawing frozen food, it can be suitably used as an absorbent sheet for a moisture removal pad for cooking ingredients that are liquid. If the liquid comes out of the food, it will look bad and reduce the taste. Furthermore, when the absorbed sheet becomes uneven, the visual impression is poor. In particular, the appearance is important for products.

  When the absorbent resin touches the food, it will spill liquid from the food, reducing its taste. Therefore, it is essential that the absorbent resin is not detached and does not come out on the surface, and it is preferable that the absorbent resin and the food in the absorber structure do not exchange moisture. In the absorption sheet of this invention, this can be achieved by providing the layer which does not have an absorptive resin in the surface which contacts food. Furthermore, the odor can be reduced.

  The absorbent sheet of the present invention can also be suitably used as an absorbent sheet for a mask. Various masks are commercially available, but usually have a structure that stops foreign matter with the fineness of the fibers, and it is difficult to completely stop fine things such as pollen. The ability to stop pollen and the like is enhanced by using the water-absorbing absorbent sheet of the present invention as a mask. In the mask, if there is a portion where the absorbent resin does not exist or if the degree of absorption varies depending on the location, the ability to stop pollen will vary, which is not preferable. The absorbent sheet of the present invention can be preferably used because it absorbs uniformly throughout. Naturally, there is a problem that the feel is poor if the absorbent resin is detached, but such a problem does not occur in the absorbent sheet of the present invention.

  The absorbent sheet of the present invention can be suitably used as an absorbent sheet for water-wetting prevention pads of electronic devices. Precision devices such as personal computers and digital cameras are not only damaged by water but also have a problem of data loss. Therefore, it is particularly required to prevent water from getting wet when liquid is accidentally spilled. Since it is difficult to cover all precision parts with a waterproof sheet, an absorbent sheet can be suitably used.

  In the conventional absorbent sheet, the desorbed absorbent resin enters into the components, which causes a problem, but the absorbent sheet of the present invention can be preferably used because it does not have a desorbing component. In addition, since electronic devices have a certain value for miniaturization, there is almost no space for absorbing liquid and swelling. If only a part is absorbed to form a weir, it is a problem that it will not be absorbed any more, and it is required to absorb the whole like the absorbent sheet of the present invention.

  Specific examples and comparative examples of the present invention are shown below, but the present invention is not limited to the following examples. The following measurements are performed in an environment of 25 ° C. and 50% RH unless otherwise specified. In addition, the density | concentration of the physiological saline used for a measurement is 0.9 mass%.

(1) Measurement of absorption capacity of absorbent resin under no pressure; Tea-bag method Absorbent resin A (g) (about 0.05 g) is uniformly placed in a non-woven tea bag bag (60 × 40 mm) Immerse in physiological saline at 23 ° C. After 180 minutes, the bag is taken out, the corner of the tea bag is fixed, suspended for 10 minutes in an oblique state, drained, and then the mass B (g) of the tea bag is measured. The same operation as a blank was performed for the absorbent resin, and the mass C (g) was measured. The absorption rate is calculated according to (Equation 4). The measurement is performed three times, and the average value is taken as the absorption magnification. From these values, the absorption capacity was determined from the following equation.
Absorption capacity (g / g) = (B (g) -C (g)) / A (g)

(2) Measurement of absorption rate of absorbent resin; vortex method 50 g of physiological saline adjusted to 25 ° C. was measured in a 100 ml glass beaker. A 30 × 8 mm rotator was placed here, placed on a magnetic stirrer with a tachometer, and rotated at 600 rpm. The rotation speed was confirmed with a non-contact tachometer. 2.00 g of the absorbent resin was measured and put into a beaker. The time from when the absorbent resin was added until the liquid surface became flat was taken as the absorption time.

(3) Measurement of neutralization rate of carboxyl group of absorbent resin outer surface and central part (i) Measuring device FTS-575 manufactured by Bio-Rad was used as a measuring device.
(Ii) Measurement condition microscopic ATR method (crystal plate Ge, single reflection)
Back Ground: Air, normal temperature measurement aperture: 50 × 50 μm
Number of integration: 100 times above 1,695 cm ^-1 (carboxylate ν _{C = O,} baseline 1774~1616cm ^-1) from the spectral data obtained by measurement conditions and 1558cm ^-1 (carboxylate [nu _COO-, baseline 1616～ The peak area ratio (1695/1558 cm ⁻¹ ) of 1500 cm ⁻¹ ) was determined.
(Iii) Preparation of calibration curve Partially crosslinked polyacrylic acid obtained by neutralizing 10 mol%, 30 mol%, 50 mol%, 70 mol%, 90 mol%, 100 mol% of the total carboxylic acid with ammonia was used as a sample for preparing a calibration curve. The calibration curve sample was cleaved, and the central portion was measured five times per sample by the microscopic ATR method. A calibration curve (5th order polynomial approximate curve) was created from the -COOH / -COO-peak area ratio. The cleaving was performed with an ultramicrotome (ULTRACUT N manufactured by Reichert).
(Iv) Measurement of sample Measurement was performed in the same manner as the calibration curve sample. The outer surface of the absorbent resin was directly measured by the ATR method, and the central portion of the absorbent resin was cleaved by an ultramicrotome and then measured by the ATR method. The outer surface of the absorbent resin was measured 3 times per sample, and the central portion of the absorbent resin was measured 5 times per sample, and the average value was taken as the measurement result.

(4) Measurement of residual monomer of absorbent resin 1 g of absorbent resin was precisely weighed into a 300 ml beaker, 250 g of physiological saline was added, and the mixture was stirred for 6 hours. After a predetermined time, the membrane was filtered through a membrane filter, and the filtrate was analyzed by high performance liquid chromatography. The analysis conditions of high performance liquid chromatography are as follows.
Column: Tosoh, ODS80Ts
Column temperature: 40 ° C
Carrier: 10 mM phosphoric acid aqueous solution, flowed at 0.7 ml / min Detection: UV 207 nm
Driving amount: 50 μl

(5) Measurement of absorption capacity of absorbent resin under pressure Cylindrical instrument made of acrylic resin (outer diameter 35.0mm, inner diameter 24.5mm, height 30mm, weight D ( to g)), the absorbent resin E (g) (placed to be about 0.16 g) of uniform, nothing put as weight in 0.0 g / cm ^2, 278 as a weight in 57 g / cm ^2. A 3 g weight (outer diameter 24.5 mm) was placed. 60 ml of physiological saline was placed in a petri dish made of SUS (inner diameter: 120 mm), and a cylindrical instrument was placed therein for 1 hour. After a predetermined time, draining was performed with a paper towel, and the mass F (g) of the entire instrument was measured with a balance. From the obtained value, the absorption capacity under pressure was determined by the following formula.
Absorption capacity (g / g) = (F (g) −D (g) −weight of weight (g)) / E (g)

(6) Measurement of water retention ratio of absorbent resin “Water retention ratio” represented by the following formula was used as an index indicating the water retention capacity of the absorbent resin. The tea bag including the water-absorbing absorbent resin immediately after the above-described Tea-bag method was carried into a centrifuge, dehydrated at 250 G for 3 minutes, and the mass was measured. The same operation was performed without using the absorbent resin, and the mass was measured to obtain a blank. From these values, the water retention magnification was calculated according to the following formula. The measurement was performed three times, and the average value was taken as the water retention magnification.
Water holding capacity of absorbent resin (g / g) = {(mass of tea bag after absorption with centrifugal separator after absorption) − (mass of blank tea bag after absorption) − (mass of absorbent resin)} / ( Absorbent resin mass)

(7) Measuring device for surface strength of absorbent resin: Shimadzu Autograph AG-1
Sample: 0.10 g of an absorbent resin was precisely weighed and placed uniformly in the bottom of a cylindrical container having an inner diameter of 20.5 mm and a height of 50 mm, with a nylon sheet having a pore diameter of 75 μm attached to the bottom surface. A 50φ petri dish was prepared, 0.90 g of physiological saline was added, and the cylindrical container containing the absorbent resin was left to stand for absorption swelling for 1 hour.
Measurement: A 1 kN load cell was used, and a cylindrical shaft having a diameter of 19.7 mm was attached. The measurement range was set to 0.2 kN, and the load cell was set to a height at which no load was applied, and from there, it was set to decrease at a constant speed of 0.6 mm / min. The pressure applied to the load cell was recorded over time. Here, the surface strength represents the load (N) when the actual volume is reached. The actual volume of the absorbent resin was calculated from the specific gravity of physiological saline 1.010 g / cm ³ and the specific gravity of the absorbent resin.

(8) Measurement of sheet absorption capacity and absorption capacity of absorbent resin in the sheet The absorption capacity of the sheet was measured by the T-Bag method in the same manner as the absorbent resin. The absorption capacity of the absorbent resin in the sheet was calculated by the following formula by measuring the absorption capacity of an equivalent sheet except that the absorbent resin was not included, making it a blank.
Absorption capacity of absorbent resin in sheet (g / g) = {(mass of sheet after absorption) − (mass of blank sheet after absorption) − (mass of absorbent resin in sheet)} / (sheet Absorbent resin mass)

(9) Measurement of sheet absorption speed, diffusion length, and rewet amount The sheet was cut into a rectangle of 160 mm in length and 70 mm in width and allowed to stand on a table. Here, 15 g of colored physiological saline was dropped over 1.5 seconds. The surface of the absorber was carefully observed, and the time from the start of dropping to the absorption and absorption of the liquid on the surface of the sheet was measured to obtain the absorption rate (seconds). The length at which the liquid diffused 3 minutes after the start of dropping was measured and defined as the diffusion length (mm). Five minutes after the start of dropping, a square filter paper having a length of 100 mm and a width of 100 mm whose mass was measured in advance was placed on the dropping position, and a 3.5 kg weight having the same bottom area as the filter paper was placed thereon. The weight was removed 3 minutes after placing the filter paper, and the mass of the filter paper was measured. The mass increase of the filter paper was defined as the rewet amount (g).

(10) Desorption test After completely absorbing 200 g / m ² of physiological saline, hold the edge of the sheet by hand, and with the sheet vertical, at a speed of reciprocating 30 cm in width per second. At the time of 10 reciprocations, it was judged visually whether or not the absorbent resin was substantially collapsed, moved or detached. After completely absorbing the liquid of 500 g / m ² , the shape of the sheet changes when the absorption part is held by hand and the width of 20 cm is reciprocated 10 times at a speed of 1 reciprocation per second. Judgment was made by looking at whether or not there was. Furthermore, after immersing completely in physiological saline and reaching saturation swelling, the same test is performed, and it is judged by checking whether or not the absorbent resin has substantially collapsed, moved, detached, or the sheet shape has not collapsed. did.

(11) Evaluation of bending resistance The bending resistance was evaluated according to the bending resistance D method (heart loop method) described in JIS standard L1096.

(12) Short-time rewet method An absorber having a predetermined size is prepared. If not in the form of a sheet, uniformly spread a predetermined amount of composite, absorbent resin, hydrophilic fiber, etc. over a predetermined area, and then collect it from Unicharm's “Lifely Refreshing Pat 20cc” The surface sheet thus prepared was placed, and the four corners were stuck and fixed with a cellophane tape to obtain an absorber. 5 cc of physiological saline was dropped on the absorbent for 5 seconds, and 30 seconds later, a filter paper having been weighed in advance was placed on the absorbent, and a weight of 1.96 kg was placed on the filter paper. After leaving in this state for 10 seconds, the filter paper was removed, the filter paper was weighed, and the mass increased from the original mass was taken as the rewet amount. In this measurement, since the time to measurement is short, the measured value is an index of the absorption rate.

(13) Long-time rewet method The measurement was performed in the same manner as the short-time rewet method, except that the filter paper was placed 10 minutes after the liquid was dropped. In this measurement, since sufficient time can be taken for absorption, it becomes an index of dry feeling.

(14) Average particle diameter of hydrophilic fiber The hydrophilic fiber dispersed in water as a dispersion medium was treated with ultrasonic waves for 1 minute, and the volume-based median diameter at 25 ° C was measured. The measurement was performed using a laser diffraction / scattering particle size distribution meter (LA-910, manufactured by Horiba, Ltd.). The average particle diameter was calculated as the number average of volume frequency.

(15) Average particle diameter of the absorbent resin The opening of the absorbent resin is 20 μm, 25 μm, 32 μm, 38 μm, 45 μm, 53 μm, 63 μm, 75 μm, 90 μm, 106 μm, 212 μm, 300 μm, 425 μm, 500 μm, 600 μm, 710 μm, Using a sieve of 850 μm, 1000 μm, 1180 μm, 1400 μm, 1700 μm and 2500 μm, sieving was carried out for 10 minutes using a low tap type sieve shaker. The intermediate value between the opening of the sieve that can pass and the opening of the sieve that cannot pass is taken as the particle size, and for each particle size, the particle size and the particle size in the entire absorbent resin The product of the mass ratio was determined, and the sum of all the products was calculated as the average particle size. In addition, about what passed the 20 micrometers sieve, it was 10 micrometers, and it was 2700 micrometers about what remained on the 2500 micrometers sieve.

(16) Evaluation of Absorption of Protein-Containing Aqueous Solution The weight of a non-woven tea bag bag (70 × 90 mm) is measured. Weigh 0.2 g of absorbent resin or composite and place in a tea bag. A Saran Wrap (registered trademark) is placed in an appropriate size on a hot plate adjusted to 37 ° C., and a tea bag containing a sample is placed thereon. In the tea bag, the sample is uniformly placed on a 30 mm × 30 mm square. 2 g of bovine defibrinated blood temperature-controlled at 37 ° C. is weighed with a syringe and fed to the center of the sample (registered trademark) over 2 seconds. Immediately after feeding, in order to prevent blood from clotting by air, a Saran wrap (registered trademark) is put over the entire upper surface of the tea bag. At this time, be careful not to let the sample or the fed blood touch the air. After feeding the blood, 4 minutes later, Saran Wrap (registered trademark) is removed and sandwiched between 10 kimwipes, and the unabsorbed blood is absorbed by the kimwipes by applying a load. Thereafter, the weight of the tea bag is measured. On the other hand, the same measurement is performed using a tea bag that does not contain a sample, and this is used as a blank.
Absorption capacity is calculated by the following formula.
Absorption magnification = (weight after absorption (g) −sample weight (g) −weight of tea bag (g) * weight after absorption of blank tea bag (g) / original weight of blank tea bag (g ) / Sample weight (g)

(17) Suction evaluation of protein-containing aqueous solution 0.2 g of sample is weighed in a non-woven tea bag bag (70 × 90 mm). A Saran Wrap (registered trademark) is placed in an appropriate size on a hot plate adjusted to 37 ° C., and a tea bag containing a sample is placed thereon. 1.0 g of bovine defibrinated blood whose temperature has been adjusted to 37 ° C. in advance is weighed with a syringe and fed to the center of the sample over 2 seconds. Observe the absorption state as it is. As the blood on the tea bag is absorbed, it can be observed that the color of the part on the tea bag becomes lighter. The most absorbed at the time after 2 minutes is judged as ◎, the one that is absorbed about 70% is judged as ◯, the one that is absorbed but small in quantity is △, and the one that is hardly absorbed is judged as ×. .

[Production Example 1] (Preparation of ammonium acrylate by neutralization of acrylic acid)
Acrylic acid manufactured by Wako Pure Chemical Industries, Ltd. was used as a reagent special grade. Acrylic acid was used after distillation before use to remove the polymerization inhibitor. Next, 100 kg of acrylic acid was dissolved in 297.22 kg of water. The aqueous solution was cooled in an ice bath, and while maintaining the liquid temperature at 30 ° C. or lower, 75.56 kg of a 25 mass% aqueous ammonia solution was gradually added with stirring to obtain a 40 mass% 80 mol% neutralized ammonium acrylate aqueous solution. It was.

[Production Example 2] (Preparation of sodium acrylate by neutralization of acrylic acid)
Acrylic acid manufactured by Wako Pure Chemical Industries, Ltd. was used as a reagent special grade. Acrylic acid was used after distillation before use to remove the polymerization inhibitor. Next, 100 kg of acrylic acid was dissolved in 43.2 kg of water. This aqueous solution was cooled in an ice bath, and while maintaining the liquid temperature at 30 ° C. or lower, 166.7 kg of a 25% by mass sodium hydroxide aqueous solution was gradually added with stirring, and 40% by mass of 75 mol% neutralized sodium acrylate An aqueous solution was obtained.

[Production Example 3]
300 kg of the monomer aqueous solution of Production Example 1 and 0.024 kg of trimethylolpropane triacrylate were added. Subsequently, as a photopolymerization initiator, 0.0067 kg of 2,2-dimethoxy-1,2-diphenylethane-1-one and 0.0033 kg of ammonium persulfate were added, and the aqueous monomer solution was cooled to 10 ° C., The reaction system was purged with nitrogen by bubbling with nitrogen gas. The dissolved oxygen was 1 ppm or less. This aqueous solution is irradiated with ultraviolet rays for 2 minutes using a high-pressure mercury lamp (MENK-20-25XE, 20W, emission length 253 nm; three units of this manufactured by SEN EngineeringCO., Ltd.) using an aqueous solution having a thickness of 20 mm. (Light quantity 684 mJ / cm ² ). The internal temperature started from 13 ° C and the maximum temperature reached was about 90 ° C. Thereafter, the gel was taken out and coarsely crushed, and then dried for 2 hours using a 130 ° C. hot air dryer. After drying, the mixture was pulverized with a homogenizer. This absorbent resin was designated as an absorbent resin (1).

[Production Example 4]
To 25 kg of the absorbent resin (1), 0.125 kg of ethylene glycol diglycidyl ether, 3 kg of water and 0.3 kg of silica were added and mixed as a crosslinking agent. This was vacuum dried at 25 ° C. This was designated as absorbent resin (2).

[Production Example 5]
Absorbent resin (2) was heated for 10 minutes using a 180 degreeC hot-air dryer. This absorbent resin was designated as an absorbent resin (3).

[Production Example 6]
300 kg of 40 mass% ammonium acrylate aqueous solution of Production Example 2 and 0.024 kg of trimethylolpropane triacrylate were added. Subsequently, as a photopolymerization initiator, 0.0067 kg of 2,2-dimethoxy-1,2-diphenylethane-1-one and 0.0033 kg of ammonium persulfate were added, and the aqueous monomer solution was cooled to 10 ° C., The reaction system was purged with nitrogen by bubbling with nitrogen gas. The dissolved oxygen was 1 ppm or less. This aqueous solution is irradiated with ultraviolet rays for 2 minutes using a high-pressure mercury lamp (MENK-20-25XE, 20W, emission length 253 nm; three units of this manufactured by SEN EngineeringCO., Ltd.) using an aqueous solution having a thickness of 20 mm. (Light amount 684 mJ / cm @ 2). The internal temperature started from 13 ° C and the maximum temperature reached was about 90 ° C. Thereafter, the gel was taken out and coarsely crushed, and then dried for 2 hours using a 130 ° C. hot air dryer. After drying, the mixture was pulverized with a homogenizer. This absorbent resin was designated as an absorbent resin (4).

[Production Example 7]
To 25 kg of the absorbent resin (4), 0.125 kg of ethylene glycol diglycidyl ether, 3 kg of water and 0.3 kg of silica were added and mixed as a crosslinking agent. This was vacuum dried at 25 ° C. This was designated as absorbent resin (5).

[Production Example 8]
Absorbent resin (5) was heated for 10 minutes using a 180 degreeC hot-air dryer. This absorbent resin was designated as an absorbent resin (6).

  About each absorptive resin, the thing of the average particle diameter of 106-300 micrometers was acquired by sieving. The performance is shown in Table 1 below. The performance of the absorbent resin is changed by heating. With respect to the absorbent resins (3) and (6), preferred heating conditions are set for use in general absorbents. In the present invention, there is a heating step during the manufacture of the composite. However, when dehydrated and dried in contact with the hydrophilic fibers, the hydrophilic fibers and the absorbent resin are directly bonded. At the time of composite production, it is possible to exhibit high performance by heating at low temperature and short time, compared to the case of the absorbent resin alone, due to the effect of the hydrophilic fibers due to the absence of contact between the absorbent resins. it can. At this time, the neutralization rate of the outer surface of the absorbent resin is also efficiently reduced. That is, when the absorbent resin (1) or (2) is used, the absorbent resin (3) and the absorbent resin (4) or (5) are used. The neutralization rate is comparable. As in the case of the absorbent resin (3), when the neutralization rate is below a certain level, the volatilization rate of ammonia becomes slow and the salt concentration hardly decreases.

[Example 1]
500 g of powdered cellulose manufactured by Nippon Paper Chemical Co., Ltd., K-50 floc (industrial grade) W-50GK, and 1000 g of absorbent resin (1) that passed through a 300 μm sieve but did not pass through a 90 μm sieve, Henschel Stir well into a mixer. While stirring, 500 g of water was made into a mist and sprayed. This was taken out and heated at 140 ° C. for 10 minutes under a nitrogen stream in an inert oven. This is designated as composite (1).
While the composite (1) was again stirred with a Henschel mixer, a solution obtained by dissolving 10 g of ethylene glycol diglycidyl ether in 6 kg of isopropyl alcohol was sprayed and mixed. This was heated in an inert oven at 150 ° C. for 10 minutes under a nitrogen stream. This is designated as composite (2).
An optical micrograph of the composite (2) is shown in FIG. There is no aggregation of the absorbent resins, and the fibers completely surround the absorbent resin and are directly bonded. The average particle diameter of the hydrophilic fiber was 44 μm, and the average particle diameter of the absorbent resin was 188 μm. When blood absorption characteristics were measured using this composite, the absorption ratio was 7.9, and the suction force was ◎.

[Example 2]
A composite was produced in the same manner as in Example 1 except that the absorbent resin (4) was used and the amount of ethylene glycol diglycidyl ether was changed to 7 g. This is designated as composite (3). Regarding the blood absorption characteristics, the absorption ratio was 7.3, and the suction force was ◎.

[Comparative Example 1]
The same method as in Example 1 was performed except that water was not used. Since water was not present, the hydrophilic fiber and the absorbent resin hardly adhered. After separating the absorbent resin and the powdered cellulose, the absorbent resin and the powdered cellulose were uniformly mixed again at a weight ratio of 2: 1, and the blood absorption characteristics were measured. The absorption ratio was 4.8 and the suction force was x. Met.

[Comparative Example 2]
The composite (1) in Example 1 is referred to as Comparative Example 2. Since the surface layer was not cross-linked, blood absorption characteristics were poor, the absorption capacity was 6.5, and the suction force was x.

[Comparative Example 3]
500 g of powdered cellulose manufactured by Nippon Paper Chemical Co., Ltd., K-50 floc (industrial grade) W-50GK, and 1000 g of absorbent resin (5) that passed through a 300 μm sieve but did not pass through a 90 μm sieve, Henschel Stir well into a mixer. While stirring, 500 g of water was made into a mist and sprayed. This was taken out and heated in an inert oven at 150 ° C. for 10 minutes under a nitrogen stream. This is designated as composite (4).
As a result of penetration of ethylene glycol diglycidyl ether to the inside, the cross-linked layer was thick, blood absorption characteristics were poor, the absorption capacity was 6.6, and the suction force was Δ.

  When transporting disposable sanitary material absorbent members such as disposable diapers, urine pads, sanitary napkins, etc., excrement disposal materials for pets such as animal sheets, pet sheets, and frozen seafood Absorbent sheet to prevent getting wet with defrosted water, or absorbent sheet for preventing water evaporation covering potted plant, absorbent sheet laid under potted plant, absorbent sheet placed around water tank, anti-condensation sheet Absorbent sheet for use in, etc., placed in a dripping area such as a receiving part of an umbrella stand, etc. to absorb water drops falling from an umbrella, etc., as a mat for a vehicle head cover, or in a helmet or hat Anti-steam mat, for example, a toilet paper sheet after defecation in a warm water-washed toilet seat (such as a Washlet (registered trademark) toilet bowl manufactured by TOTO Corporation), a roof in case of rain Absorbent mats for preventing wet floors due to rain on rainy days in event venues, absorbent mats for preventing wet floors on vehicles such as cars, trains or airplanes on rainy days, hospitals on rainy days, service areas, Absorbent mats for preventing floor wetting in department stores, hotels, stores, office buildings or leisure facilities, absorbent mats for preventing wetting in refrigerators, absorbent mats for preventing floor wetting in kitchens, and kitchens or kitchens Absorbent sheet for drip absorption of raw garbage, water supply equipment, hot water supply equipment or absorbent mat for floor wetting provided with sanitary ware such as toilet or toilet, absorbent mat for prevention of floor wetting around refrigerator, leisure Mats or massage therapy sheets, auxiliary mats for beds, packaging materials having water retention or humidity control functions for vegetables, fruits and flowers, fresh fish, raw meat, Packaging materials with water retention or humidity control functions such as vegetarian food or lunch boxes, packaging materials for seeds, strains, seedlings or bulbs, machinery and window cleaning, ceilings, walls, floors or windows of buildings As a waste cloth or rag for wiping off condensation and wetness, etc., it has industrial applicability, such as for preventing water evaporation during cultivation of horticultural plants.

DESCRIPTION OF SYMBOLS 1 ... Stretch nonwoven fabric, 10 ... Composite fiber, 11 ... Stretch fiber, 11a-11f ... Exposed part of stretch fiber, 12 ... Non-stretch fiber, 21, 22 ... Hopper, 23, 24 ... Extruder, 25 ... Die, 25a ... Nozzle opening, 25b ... Central opening, 25c ... Side opening, 26 ... Cooling chamber, 27 ... Air blower, 28 ... Collection conveyor, 28a ... Pulley, 28b ... Endless belt, 29 ... Suction box, 30 ... Suction blower, 31 ... guide roller, 32 ... hot embossing roller, 33 ... nip roller, 34 ... winder roller.

Claims (11)

A composite comprising hydrophilic fibers and an absorbent resin and having the following characteristics.
(1) The hydrophilic fiber and the absorbent resin are directly bonded.
(2) The absorbent resin is surface-crosslinked.   The composite according to claim 1, wherein the absorbent resin has an acid group.   2. The composite according to claim 1, wherein the surface of the absorbent resin is hydrophobic. The manufacturing method of the composite material comprised from the absorptive resin which has a hydrophilic fiber and an acid group including the following process.
(A) A step of bringing a hydrophilic fiber and an absorbent resin into contact and dehydrating and drying the hydrophilic fiber and the absorbent resin in the presence of water to obtain a composite precursor.
(B) A step of adding a compound having two or more functional groups capable of reacting with an acid group to the composite precursor.
(C) A step of performing a crosslinking reaction with the compound by heating.   The method for producing a composite according to claim 4, wherein the surface strength of the absorbent resin before dehydration drying is 0.1 to 5.5N.   6. The method for producing a composite according to claim 4 or 5, wherein the steps (B) and (C) are performed with a moisture content of 20% or less based on the weight of the water-absorbent resin.   An absorbent sheet, wherein the composite according to any one of claims 1 to 3 is adhered to a substrate with an adhesive.   An absorbent sheet comprising the composite according to any one of claims 1 to 3 and a thermoplastic fiber, wherein the thermoplastic fiber is formed into a sheet by heat-sealing.   The composite according to any one of claims 1 to 3 is brought into contact with a thermoplastic fiber, and is formed into a sheet by heating with hot air having a wind speed of 0.1 to 100 m / s and a temperature of 70 ° C to 180 ° C. Manufacturing method of absorbent sheet.   An absorbent article comprising the absorbent sheet according to claim 7 or 8 and an auxiliary member.   The manufacturing method of an absorbent article according to claim 10, wherein the manufacturing process of the absorbent sheet and the mounting process of the auxiliary member are performed on the same line.