JP7146641B2 - Textile processing agent and liquid-permeable nonwoven fabric containing the same - Google Patents

Description

The present invention provides a fiber processing agent capable of imparting excellent rewetting properties and repeated water permeability to a nonwoven fabric, a liquid-permeable nonwoven fabric containing the fiber processing agent, and a sanitary fabric using the liquid-permeable nonwoven fabric. Regarding materials.

In recent years, the spread of disposable diapers and sanitary napkins has been remarkable, and the required quality and performance have been improving. For example, wearing disposable diapers does not necessarily treat excrement once, and it is necessary to avoid discomfort caused by excretion several times. In addition to rapid liquid permeability (initial water permeability), particularly low rewetting (rewetting property) and durability of water permeability performance (repeated water permeability) are strongly required.

In order to meet these demands, for example, Patent Document 1 below proposes a polyolefin nonwoven fabric provided with a hydrophilic treatment agent containing a specific polyether and polyether-modified silicone. However, although the polyolefin-based nonwoven fabric described in Patent Document 1 has good initial water permeability, it is still insufficient in rewetting property and repeated water permeability.

JP-A-10-53955

In view of the problems of the prior art described above, the problem to be solved by the present invention is a fiber processing agent capable of improving the rewetting property and repeated water permeability of a nonwoven fabric, and a fiber comprising the fiber processing agent to which the fiber processing agent is applied. It is to provide a nonwoven fabric that is

In order to solve this problem, the present inventors conducted extensive studies and repeated experiments, and found that a specific component (A) represented by the general formula (1) and a specific component (A) represented by the general formula (2) By using B) in combination, the balance between hydrophilicity and hydrophobicity is maintained, affinity for nonwoven fabric and affinity for body fluids such as urine are compatible, and excellent initial water permeability, rewetting property, and repeated water permeability. The inventors have found that a nonwoven fabric can be provided, and have completed the present invention.

That is, the present invention is as follows.
[1] the following general formula (1):
HO—(A ¹ O) _p —H General formula (1)
{In the formula, A ¹ is an alkylene group having 2 to 4 carbon atoms, and p is an integer of 1 to 3. } and the following general formula (2) different from the component (A):
R ¹ —O—(A ² O) ₁ —{C(O)R ² C(O)—O—(A ³ O) _m } _n —R ³ General formula (2)
{In the formula, R ¹ and R ³ are each independently a hydrogen atom, an alkyl group having 1 to 24 carbon atoms, an alkenyl group having 2 to 24 carbon atoms, an alkanoyl group having 2 to 24 carbon atoms, or an alkanoyl group having 2 to 24 carbon atoms. where only one of R ¹ and R ³ is non-hydrogen is a mono-form, and where both R ¹ and R ³ are non-hydrogen is a di-form, the mono-form and the ratio of the di-form is mono-form: di-form = 10:0 to 1:9, and R ² is an alkylene group having 1 to 12 carbon atoms, an alkenylene group having 2 to 12 carbon atoms or an alkenylene group having 6 to 12 carbon atoms. is an arylene group, A ² and A ³ are each independently an alkylene group having 2 or 3 carbon atoms, l is an integer of 10 to 200, m is an integer of 39 , and n is an integer of 0 or 1-2 . provided that either one of R ¹ and R ³ is an alkyl group having 1 to 24 carbon atoms, an alkenyl group having 2 to 24 carbon atoms, an alkanoyl group having 2 to 24 carbon atoms, or an alkenoyl group having 2 to 24 carbon atoms; and l+n is 1 or more, and not all of A ² and A ³ are alkylene groups having 2 carbon atoms. } component (B) represented by; and component (C) which is a polyether-modified silicone;
and the component (C) is 10% by mass to 30% by mass with respect to the total amount of the component (A) and the component (B).
[2] A liquid-permeable nonwoven fabric in which the amount of the fiber processing agent described in [1] above is 0.1 to 1.5% by weight.
[3] The liquid-permeable nonwoven fabric according to [2], wherein the liquid-permeable nonwoven fabric is a nonwoven fabric made of thermoplastic fibers.
[4] The liquid-permeable nonwoven fabric according to [2] or [3], wherein the nonwoven fabric is composed of fibers having a fineness of 0.45 to 5.0 dtex.
[5] The liquid-permeable nonwoven fabric according to any one of [2] to [4], wherein the nonwoven fabric is a long-fiber nonwoven fabric.
[6] The liquid-permeable nonwoven fabric according to any one of [2] to [5], wherein the repeated water permeability of the liquid-permeable nonwoven fabric is 70% or more at the fourth time.
[7] The liquid-permeable nonwoven fabric according to any one of [2] to [6], wherein the liquid-permeable nonwoven fabric has a rewetting property of 0.5 g or less.
[8] A sanitary material using the liquid-permeable nonwoven fabric according to any one of [2] to [7].

Since the nonwoven fabric coated with the fiber processing agent according to the present invention has excellent initial water permeability, rewetting property, and repeated water permeability, it can be used as a top sheet or second sheet for sanitary materials such as sanitary napkins, incontinence pads, and disposable diapers. Alternatively, for example, masks, body warmers, tape bases, patch bases, emergency bandages, packaging materials, wipe products, medical gowns, bandages, clothing, skin care sheets, etc. It can be used preferably.

BEST MODE FOR CARRYING OUT THE INVENTION Hereinafter, embodiments of the present invention will be described in detail.
The fiber processing agent of this embodiment has the following general formula (1):
HO—(A ¹ O) _p —H General formula (1)
{In the formula, A ¹ is an alkylene group having 2 to 4 carbon atoms, and p is an integer of 1 to 3. } and the following general formula (2) different from the component (A):
R ¹ —O—(A ² O) ₁ —{C(O)R ² C(O)—(A ³ O) _m } _n —R ³ General formula (2)
{In the formula, R ¹ and R ³ are each independently a hydrogen atom, an alkyl group having 1 to 24 carbon atoms, an alkenyl group having 2 to 24 carbon atoms, an alkanoyl group having 2 to 24 carbon atoms, or an alkanoyl group having 2 to 24 carbon atoms. or —C(O)—R ⁴ —COOX (wherein R ⁴ is an alkylene group having 1 to 12 carbon atoms, an alkenylene group having 2 to 12 carbon atoms, or an arylene group having 6 to 12 carbon atoms. , and X is a hydrogen atom or an anion); R ² is an alkylene group having 1 to 12 carbon atoms, an alkenylene group having 2 to 12 carbon atoms or an arylene group having 6 to 12 carbon atoms; ² and A ³ are each independently an alkylene group having 2 to 4 carbon atoms, l is 0 or an integer of 1 to 1000, m is 0 or an integer of 1 to 1000, and n is an integer of 0 or 1-100. However, l+n is 1 or more. } Component (B) represented by;
contains

First, the component (A) represented by general formula (1) will be described.
In general formula (1), A ¹ is an alkylene group having 2-4 carbon atoms, and p is an integer of 1-3. A ¹ is an alkylene group having 2 to 4 carbon atoms, preferably an alkylene group having 3 to 4 carbon atoms, more preferably 3 carbon atoms, from the viewpoint of rewetting property and repeated water permeability. p represents the degree of polymerization of the alkyleneoxy group represented by (A ¹ O) and is an integer of 1 to 3, but from the viewpoint of rewetting property and repeated water permeability, 1 to 2 is preferable, and 1 is more preferable.

Component (A) is, for example, an alkylene glycol having 2 to 4 carbon atoms, such as ethylene glycol, propylene glycol, and butylene glycol, in the presence of a base catalyst, at 80 to 200° C., ethylene oxide, propylene oxide, butylene oxide, and the like. It can be obtained by adding an alkylene oxide having 2 to 4 carbon atoms. Examples of basic catalysts that can be used include potassium hydroxide and sodium hydroxide. Commercially available ethylene glycol, propylene glycol, butylene glycol, diethylene glycol, dipropylene glycol, dibutylene glycol, triethylene glycol, tripropylene glycol, tributylene glycol, etc. may be used.

In general formula (2), R ¹ and R ³ each independently represent a hydrogen atom, an alkyl group having 1 to 24 carbon atoms, an alkenyl group having 2 to 24 carbon atoms, an alkanoyl group having 2 to 24 carbon atoms, or an alkanoyl group having 2 to 24 carbon atoms. 2 to 24 alkenoyl groups or —C(O)—R ⁴ —COOX (wherein R ⁴ is an alkylene group having 1 to 12 carbon atoms, an alkenylene group having 2 to 12 carbon atoms, or an arylene group having 6 to 12 carbon atoms and X is a hydrogen atom or an anion), and R ² is an alkylene group having 1 to 12 carbon atoms, an alkenylene group having 2 to 12 carbon atoms, or an arylene group having 6 to 12 carbon atoms. and A ² and A ³ are each independently an alkylene group having 2 to 4 carbon atoms, l is 0 or an integer of 1 to 1000, m is 0 or an integer of 1 to 1000, n is 0 or an integer from 1 to 100; However, l+n is 1 or more, and the component (B) is a compound different from the component (A). do.

From the viewpoint of wettability and repeated water permeability, either one of R ¹ and R ³ is an alkyl group having 1 to 24 carbon atoms, an alkenyl group having 2 to 24 carbon atoms, an alkanoyl group having 2 to 24 carbon atoms, or An alkenoyl group having 2 to 24 carbon atoms is preferred. In this case, the number of carbon atoms is preferably 8-22, more preferably 12-18, from the same viewpoint. These alkyl groups, alkenyl groups, alkanoyl groups and alkenoyl groups may be linear or branched.

A ² and A ³ are each independently an alkylene group having 2 to 4 carbon atoms, but from the viewpoint of rewetting properties, repeated water permeability, and stability in working baths, they should be alkylene groups having 2 to 3 carbon atoms. is preferred.
From the same point of view, the polyalkyleneoxy groups represented by (A ² O) _l and (A ³ O) _m are an alkyleneoxy group having 2 carbon atoms (ethyleneoxy group) and an alkyleneoxy group having 3 carbon atoms. (Propyleneoxy group) is more preferably used in combination. In this case, the molar ratio of the ethyleneoxy group to the propyleneoxy group is preferably ethyleneoxy group:propyleneoxy group = 5:95 to 50:50, more preferably 5:95 to 40:60, and 10:90. ~30:70 is more preferred.

When the polyalkyleneoxy group represented by (A ² O) ₁ and (A ³ O) _m consists of a plurality of alkyleneoxy groups, the addition method may be block addition or random addition. l and m respectively represent the degree of polymerization of the polyalkyleneoxy groups represented by (A ² O) _l and (A ³ O) _m , l represents 0 or an integer of 1 to 1000, m is 0 Alternatively, it represents an integer of 1 to 1000, but both l and m are preferably 10 to 200 from the viewpoint of rewetting property and repeated water permeability.
Moreover, the component (B) represented by the general formula (2) preferably has an average molecular weight of 100,000 or less from the viewpoint of ease of handling.

Examples of the component (B) include polyalkylglycols (B1), polyoxyalkylene alkyl ethers (B2), alkyleneoxy adducts of divalent carboxylic acids (B3), esters thereof (B4), and the like. be able to.
Polyalkylglycol (B1) can be obtained, for example, by adding an alkylene oxide to a dihydric alcohol. Also, the polyoxyalkylene alkyl ether (B2) can be obtained, for example, by adding an alkylene oxide to a monohydric alcohol. In this case, the reaction may be carried out at 80 to 200° C. according to a conventional method using a base catalyst such as potassium hydroxide or sodium hydroxide. Examples of dihydric alcohols include ethylene glycol, propylene glycol, and butylene glycol. Examples of monohydric alcohols include alcohols having 1 to 24 carbon atoms. Such alcohols may have branches or double bonds. As the alkylene oxide, alkylene oxides having 2 to 4 carbon atoms such as ethylene oxide, propylene oxide and butylene oxide can be used. When two or more alkylene oxides are used, the method of addition may be block or random.

The alkyleneoxy group adduct (B3) of divalent carboxylic acid can be obtained, for example, by adding alkylene oxide to divalent carboxylic acid, or by reacting divalent carboxylic acid with polyalkylene glycol.
The esterified product (B4) is, for example, the polyalkyleglycol (B1), the polyoxyalkylene alkyl ether (B2), and/or the alkyleneoxy group adduct (B3) of a divalent carboxylic acid obtained above. , a monovalent and/or divalent carboxylic acid can be obtained by reacting them at about 100 to 300° C. according to a conventional method. This reaction may be carried out without a catalyst, or with a catalyst such as sulfuric acid or p-toluenesulfonic acid.

Examples of monovalent carboxylic acids include carboxylic acids having 1 to 24 carbon atoms. Such carboxylic acids may have branches or double bonds. Examples of divalent carboxylic acids include aromatic dicarboxylic acids such as terephthalic acid, isophthalic acid and phthalic acid, and aliphatic dicarboxylic acids such as 1,4-cyclohexanedicarboxylic acid, adipic acid, sebacic acid, maleic acid and succinic acid. can be mentioned. Among these, aliphatic dicarboxylic acids are preferably used, and adipic acid and succinic acid are more preferably used from the viewpoint of rewetting property and repeated water permeability.

From the viewpoint of rewetting property and repeated water permeability, the blending ratio of component (A) and component (B) in the fiber finishing agent is component (A):component (B)=1:99-90 by mass ratio. :10 is preferred, and 5:95 to 50:50 is more preferred. If the blending ratio of component (A) is less than the lower limit, rewetting properties tend to decrease, and if the blending ratio of component (A) exceeds the upper limit, repeated water permeability tends to decrease.

In addition to the components (A) and (B), the fiber processing agent of the present embodiment may further contain a polyether-modified silicone as a component (C) that improves the initial water permeability (45-degree inclined flow length). can. From the viewpoint of rewetting property and 45-degree inclined flow length, the blending ratio of component (C) is preferably 5% by mass to 50% by mass, and 10% by mass with respect to the total amount of component (A) and component (B). % to 30% by mass is more preferable.

A commercially available polyether-modified silicone can be used as component (C). For example, Shin-Etsu Chemical Co., Ltd. KF-351A, KF-352A, KF-353, KF-355A, KF-615A, KF-642, KF-6204, KF-6011, KF-6012, KF-6013; Dow Corning SH8700, SH8410, SH8400, L-7002, FZ-2104, FZ-77, L-7604; Momentive Performance Materials Japan LLC TSF4440, TSF4441, TSF4452, SF1188A, SF1288, Silsoft840, Silsoft860 , Silsoft 870, Silsoft 875, Silsoft 880, Silsoft 895, etc. can be used. The polyether-modified silicone used as the component (C) is not particularly limited, but from the viewpoint of rewetting property, repeated water permeability and 45° inclined flow length, those having an HLB of 5 to 15 are preferably used, Moreover, one having a viscosity of 50 to 10000 cSt is preferably used.

In addition to the components (A), (B), and (C), the fiber processing agent of the present embodiment may contain other compounds depending on the desired purpose, as long as the desired effect is not impaired. I do not care. For example, various surfactants such as emulsifiers, softeners, smoothing agents, antistatic agents, and antifoaming agents can be appropriately contained.

The amount of the fiber processing agent adhered varies depending on the intended use. It is preferable to apply so as to adhere by weight %. The adherence amount of the fiber processing agent, which is a mixture of component A, component B, component C, and other compounds, is 0.10% by weight to 1% by weight in terms of the pure content (pure adherence amount) excluding a solvent such as water that dilutes the processing agent. A range of 0.50 wt % is preferred, more preferably 0.15 wt % to 1.20 wt %. If it is less than 0.05% by weight, it is difficult to obtain a satisfactory water permeability, while if it exceeds 1.50% by weight, skin rashes and eczema may occur.

When applying the fiber processing agent to the nonwoven fabric, it is also effective to directly apply each of the component (A), the component (B) and the component (C), or a mixture thereof, to the nonwoven fabric. However, it is preferable to mix them in advance, dilute them with a solvent such as water, and apply them to the nonwoven fabric as an aqueous solution of the fiber processing agent. The fiber processing agent of the present embodiment is obtained by uniformly mixing the component (A), the component (B), optionally the component (C), and the above-mentioned other compounds at a temperature equal to or higher than the melting point. be able to.
As a method for applying the fiber processing agent to the nonwoven fabric, known methods such as the dipping method, the spray method, and the coating method can be employed. good. In addition, a treatment such as a corona discharge treatment or a normal pressure plasma discharge treatment may be employed before application of the fiber processing agent, if necessary.

In order not to cause insufficient drying in the drying process that accompanies the speeding up of the nonwoven fabric manufacturing equipment, it is preferable that the amount of the aqueous solution of the fiber processing agent applied is small. The amount (% by weight) applied to the nonwoven fabric is preferably 1.0% by weight to 65% by weight, more preferably 3.0% by weight to 60% by weight, and still more preferably 5.0% by weight in any of the above application methods. % to 50% by weight. If the amount is less than 1.0% by weight, a uniform coating cannot be obtained, while if the amount exceeds 65% by weight, a large drying capacity is required, the equipment cost increases, and insufficient drying may occur. The concentration of the applied fiber processing agent is preferably 0.05% by weight to 100% by weight.

The method of applying the fiber processing agent is generally a coating method. Known coating methods include a kiss coater, a die, and the like, but it is preferable to use a gravure application method because the fiber processing agent can be uniformly applied in the width direction of the nonwoven fabric.
The handle of the gravure roll may be of a lattice type or a pyramid type, but is preferably of a slanted line type because the fiber processing agent is less likely to remain on the bottom of the gravure cell. The cell volume is preferably 5 cm ³ /m ² to 40 cm ³ /m ² . If it is less than 5 cm ³ /m ² , the coating amount is too small, making uniform coating of the fiber processing agent difficult. On the other hand, if it exceeds 40 cm ³ /m ² , the coating amount becomes too large, which causes problems such as insufficient drying in the drying process and uneven adhesion of the fiber finishing agent due to migration.
The cell depth of the gravure roll is preferably 10 μm to 80 μm, and the interval between the cells is preferably designed to be within the range of 80 mesh to 250 mesh so as to achieve the above cell volume.

The method for scraping off the liquid on the surface of the gravure roll may be a doctor blade method using a general hardened steel plate doctor or a rubber roll method using a roll with a rubber surface. In the case of the doctor blade method, the holding pressure is preferably 0.5 kg/cm to 1.0 kg/cm, more preferably 0.6 kg/cm to 0.8 kg/cm. In the case of the rubber roll method, the holding pressure is preferably 1.0 kg/cm or more and 5.0 kg/cm or less, more preferably 1.5 kg/cm or more and 3.5 kg/cm or less, within the range of rubber hardness of 60° or more and 80° or less. preferable. In any method, when the pressing pressure is within the above range, it is uniformly suppressed in the width direction of the non-woven fabric, so that the variation in the amount of the fiber processing agent applied is reduced.

In addition, a spraying method is also preferable because it can be applied to high-speed equipment, can be applied efficiently, and can easily maintain the thickness of the nonwoven fabric. As the spraying method, a known spraying method using air compression or a method of directly compressing and spraying the aqueous solution of the fiber processing agent may be used, but the rotor dampening method is preferable from the viewpoint of uniform application to the nonwoven fabric. By taking measures to prevent scattering of the textile processing agent aqueous solution during application, it is possible to apply even when the equipment is operating at high speed. The rotor dampening method is a method in which an aqueous solution of a textile processing agent is supplied onto a rotating rotor, and the aqueous solution of a textile processing agent is sprayed using the centrifugal force of the rotation of the rotor. In the rotor dampening method, the openings are limited so that the liquid particles of the aqueous solution of the textile processing agent blown by the rotation of the rotor in the direction of application can be sprayed only on the side of the nonwoven fabric to be applied, and can be uniformly applied in the width direction of the nonwoven fabric. , it is possible to adjust the spray particle diameter by the rotor rotation speed.

In the case of the rotor dampening method, for example, a rotor with a diameter of 40 mm to 100 mm is selected, and the nonwoven fabric surface to be applied and the center of the rotor are arranged so that the aqueous solution of the textile processing agent can adhere uniformly in the width direction of the nonwoven fabric to be applied. Set the distance from It is preferable to set so that half of the application distribution range sprayed from the adjacent rotor overlaps. Further, it is preferable that the rotors are arranged at equal intervals in the range of 60 mm to 220 mm in the width direction and arranged in two stages.

The point of uniform application is to ensure that the sprayed particles reach the inside of the nonwoven fabric to be applied, and the sprayed particle diameter is preferably 10 μm to 200 μm, more preferably 30 μm to 70 μm. The surface tension of the textile processing agent aqueous solution is important for forming the optimum spray particle size, and the spray particle size is calculated by the following formula:
Spray particle diameter (μm) = {100000 × √ (surface tension (N / m))} / (rotor diameter (mm) × rotor speed (rpm))
Calculated by

The temperature of the aqueous solution of the fiber processing agent in these coating methods is preferably 5° C. to 50° C., more preferably 12° C. to 40° C. from the viewpoint of uniform dispersion and stability of the solution. The viscosity of the aqueous solution of the fiber processing agent is preferably 0.5 mPa·s to 50 mPa·s, and more preferably 0.8 mPa·s to 20 mPa·s from the viewpoint of easier uniform application. If the viscosity exceeds 50 mPa·s, the permeability of the aqueous solution of the fiber processing agent into the nonwoven fabric tends to be poor, making uniform application difficult.

A conventional drying method can be used for drying after applying the textile processing agent aqueous solution, and there is no particular limitation, and a known method using convective heat transfer, conductive heat transfer, radiant heat transfer, etc. is adopted. Various drying methods such as a hot air circulation type, a hot air penetration type, an infrared heater type, a method of blowing hot air on both sides of a nonwoven fabric, and a method of introducing into a heated gas can be used.

The nonwoven fabric of this embodiment is made of thermoplastic fibers, and may be a long-fiber nonwoven fabric produced by a spunbond method or a short-fiber nonwoven fabric produced by a carding method, a wet papermaking method, or the like. However, from the viewpoint of strength and productivity, and from the viewpoint of imparting characteristics to the non-woven fabric surface structure and reducing irritation to the skin, as the fibers constituting the web, long fibers produced by the spunbond method are preferable. As used herein, long fibers refer to fibers having a fiber length of 55 mm or more. In addition, as for the form of thermoplastic fibers, not only those having a round cross section, but also those having a special shape such as a flat or Y-shaped cross section fiber, a hollow fiber, a crimped fiber, etc. can be used. It is not particularly limited.

The web may be a single layer, or a web formed by the spunbond method (S) may be laminated by spraying a melt-spun web by the meltblown method (M). From the viewpoint of productivity, the lamination state may be SS, SSS, SSSS, or SM, SMS, SMMS, SMSMS. Also, each layer may be formed with a different basis weight, fiber diameter, and fiber shape.

Methods for joining laminated webs include a method of joining using an adhesive, a method of joining with low-melting-point fibers or composite fibers, a method of melting and joining by sprinkling a hot-melt binder during web formation, needle punching, water flow, etc. Either mechanical entanglement such as entanglement with hot air or joining by hot air may be used. However, from the viewpoint of high-speed productivity, it is preferable to join by partial thermocompression bonding. For example, the web can be passed between heated embossing/flat rolls that can provide pinpoint, elliptical, diamond, rectangular, etc. bonding points. The thermocompression bonding area ratio in partial thermocompression bonding is preferably 5 to 40%, more preferably 5 to 25%, from the viewpoint of strength retention and flexibility. It is also preferable to use hot air for bonding from the viewpoint of maintaining the bulk of the nonwoven fabric and obtaining a cushioning texture that is preferred as a top sheet of sanitary materials. Any bonding method using hot air is not particularly limited, as long as it is a hot air circulation type, a hot air penetration type, or a method in which hot air is sprayed on both sides of the nonwoven fabric.

Examples of the thermoplastic resin that constitutes the thermoplastic fiber of the present embodiment include polyolefin resins such as polyethylene, polypropylene, and copolymerized polypropylene; and polyester resins such as polyethylene terephthalate, polybutylene terephthalate, polyethylene naphthalate, and copolymerized polyester. , nylon-6, nylon-66, copolymer nylon, and biodegradable resins such as polylactic acid, polybutylene succinate, polyethylene succinate, and the like, but are not particularly limited. Polyolefin-based resins are preferable from the viewpoint of texture of non-woven fabrics, and from the viewpoints of general purpose and convenience of collection, since many of the uses are disposable materials. Also, the fiber may be of one type, or a combination of two or more types of resin such as side-by-side or sheath-core.

The average fineness of fibers of the nonwoven fabric is preferably 0.45 dtex to 10.0 dtex, more preferably 0.55 dtex to 8.0 dtex, still more preferably 0.86 dtex to 5.0 dtex. From the viewpoint of spinning stability, the average fineness is preferably 0.45 dtex or more, and on the other hand, from the viewpoint of the texture of nonwoven fabrics used for sanitary materials, it is preferably 10.0 dtex or less.

The basis weight of the nonwoven fabric is preferably 8 g/m ² to 80 g/m ² , more preferably 10 g/m ² to 40 g/m ² or less, still more preferably 10 g/m ² to 30 g/m ² . A basis weight of 8 g/m ² or ^more satisfies strength as a nonwoven fabric used for sanitary materials. It tends to be difficult to give a thick impression.

The nonwoven fabric to which the fiber processing agent of the present embodiment is applied preferably has the following characteristics in order to absorb urine, body fluids, and the like without stagnation.

The repeated water permeability, which is an index of the water permeability of the nonwoven fabric of the present embodiment, is preferably 70% or more at the fourth time. Since diapers are not changed after each urination, the non-woven fabric used for the top sheet and second sheet must pass body fluids such as urine without stagnation even after repeated urination. There is If the value of the fourth repeated water permeability is less than 70%, for example, when used as a top sheet or second sheet of a disposable diaper, urine cannot pass through the second and subsequent times sufficiently, which causes urine leakage. there is a possibility.

The rewetting property, which is an index of the water permeability of the nonwoven fabric of the present embodiment, is preferably 0.5 g or less. If the rewetting property exceeds 0.5 g, for example, when the surface material is used as a surface material of a disposable diaper, when the surface material touches the skin after urinating, the surface material feels very wet, resulting in poor usability. It may cause a rash. The lower the rewetting property, the better, but a value of 0.01 g or less is the lower limit of measurement.

The 45-degree inclined flow length, which is an index of water permeability of the nonwoven fabric of the present embodiment, is preferably 30 mm or less, more preferably 25 mm or less. If the 45-degree inclined flow length exceeds 30 mm, for example, when it is used as a surface material of a disposable diaper or the like, the liquid flow on the surface increases, and urine leakage is likely to occur.

EXAMPLES The present invention will be specifically described below with reference to examples and comparative examples, but the present invention is not limited only to the following examples. The evaluation methods for each property are as follows, and the physical properties of the obtained nonwoven fabric are shown in Table 2 below. Hereinafter, the machine direction in the production of nonwoven fabric is called the MD direction, and the width direction perpendicular to that direction is called the CD direction.

1. Average fineness (dtex)
The nonwoven fabric was divided into 5 equal parts in the CD direction to obtain 1 cm square test pieces, and the diameter of each fiber was measured at 20 points with a microscope VHX-700F manufactured by Keyence Corporation, and the single filament fineness was calculated from the average value.

2. Fabric weight of nonwoven fabric (g/m ² )
According to JIS-L1906, 5 test pieces of 20 cm in the MD direction × 5 cm in the CD direction are collected so that the collection positions are even in the CD direction of the nonwoven fabric, the mass is measured, and the average value is the weight per unit area. It was calculated as a basis weight (g/m ² ) by conversion.

3. Coating amount of textile processing agent aqueous solution (% by weight)
The following formula is obtained from the consumption of the aqueous solution of the textile finishing agent for one hour during the application of the textile finishing agent aqueous solution:
Textile processing agent aqueous solution application amount (% by weight) = Textile processing agent aqueous solution consumption amount (g)/{Nonwoven fabric basis weight (g/m ² ) × width (m) × processing speed (m/min) × 60 (min)} × 100
The value calculated by was used as the coating amount (% by weight) of the textile processing agent aqueous solution.

4. The pure content adhesion amount is calculated from the application amount (% by weight) by the following formula:
The pure amount of the textile finishing agent (wt%) was calculated from the following formula: Amount of coating (wt%) x (Concentration of aqueous solution of textile processing agent (% by weight))/100.
Further, the pure coating amount of component (A) and component (B) is calculated from the coating amount (% by weight) by the following formula:
Pure attachment amount (% by weight) of component (A) and component (B) = coating amount (% by weight) x (component concentration (% by weight) of component (A) in textile finishing agent aqueous solution + component in textile finishing agent aqueous solution Component concentration of (B) (% by weight)) / 100
Calculated by

5. Rewetting property (g)
A test cloth is placed on three sheets of specific filter paper (GRADE: 989 manufactured by Ahlstrom) in order to keep the properties of the absorbent constant. Place a plate (about 800 g) with a 10 cm square hole with a diameter of 25 mm in the center on top of it, and drop physiological saline (4.0 times the weight of the absorber) from a height of 25 mm above the central hole. and absorb. Next, the plate on the test cloth is removed, and a weight of 3.5 kg (10 cm square) is gently placed on the cloth for 3 minutes to stabilize the liquid distribution in the absorbent. Next, remove the weight of 3.5 kg once, quickly place two pieces of pre-weighed filter paper for measurement (ERTMWWSSHEETS 12.5 cm square manufactured by HOLLINGSWORTH & VOSE.COMPANY) on the test cloth, and gently place the weight of 3.5 kg again. . After 2 minutes the weight gain of the measurement filter paper is weighed. The value of the increase (g) was taken as the rewetting property.

6. Repeated water permeability (%)
Ten sheets of toilet paper (Hard Single 1R55m, manufactured by Itoman Co., Ltd.) are piled up as absorbents, and a test cloth (20 cm×30 cm) is placed thereon. A stainless steel plate with 10 holes of 1.5 cm in diameter is placed on top of it, and 0.05 g of physiological saline is dripped from a height of 10 mm above the cloth located in each hole. After a minute has passed, add dropwise again in the same manner. Count the number of holes (a) that are absorbed within 10 seconds after the fourth drop. This was tested at 40 locations on the same sample, and {((a)/(10 holes×40 samples)×100)} was taken as the water permeability (%) of the fourth repetition. In addition, after the fifth drop, the number of holes (b) absorbed within 10 seconds was counted in the same manner as the fourth drop, {((b) / (10 holes x 40 samples) x 100). } was defined as the fifth repeated water permeability (%).

7.45 degree inclined flow length (mm)
10 sheets of toilet paper (Hard Single 1R55m manufactured by Itoman Co., Ltd.) are stacked as absorbers on a plate inclined at 45 degrees, and a test cloth (20 cm square) is placed on it and set at a height of 10 mm above the cloth. 0.05 g of physiological saline was added dropwise. The distance that the saline ran down from the dripping position to the end of absorption was read. This measurement was performed arbitrarily at 20 points in the test cloth, and the average value was taken as the water permeability 45° inclined flow length (mm).

<Production of nonwoven fabric (1)>
Polypropylene (PP) resin with a melt flow rate (MFR) of 55 g/10 minutes (measured at a temperature of 230°C and a load of 2.16 kg according to JIS-K7210) is spun so that the discharge amount is 0.88 g/minute・hole A filament group was extruded at a spinning temperature of 220° C. by a bond method, and the filament group was extruded toward a moving collection surface using a high-speed air jet pulling device to prepare a filament web having an average fiber diameter of 2.8 dtex.
Then, the obtained filament web was flat-rolled and embossed-rolled at a top and bottom temperature of 135° C. and a pressure of 60 kg/cm (pattern specifications: circle diameter 0.425 mm, staggered arrangement, horizontal pitch 2.1 mm, vertical pitch 1.1 mm, The line speed was adjusted so that the fibers were partially pressed against each other by passing the fibers through the compressed area ratio of 6.3%, and the target basis weight was 18 g/m ² , to obtain a long fiber nonwoven fabric (1).

<Production of nonwoven fabric (2)>
An ethylene/propylene random copolymer resin (r-PP) having an ethylene component content of 4.3 mol% and an MFR of 24 was spun-bonded at a spinning temperature of 230 at a discharge rate of 0.84 g/min.hole. ℃, and this filament group was extruded toward a moving collection surface using a high-speed pulling device with an air jet to produce a long fiber web having an average fiber diameter of 2.3 dtex. Next, using the same flat roll/embossing roll as used in the production of the nonwoven fabric (1), the obtained filament web was partially pressed against each other under the conditions of a top and bottom temperature of 135°C and a pressure of 60 kg/cm, The line speed was adjusted so that the target basis weight was 30 g/m ² to obtain a long fiber nonwoven fabric (2).

<Production of nonwoven fabric (3)>
Polypropylene (PP) with an MFR of 38 g/10 min is extruded at a spinning temperature of 240° C. and a discharge rate of 0.80 g/min·hole using a spinneret equipped with a C-shaped nozzle. Using a high-speed airflow traction device, the material was extruded toward a moving collection surface to obtain a filament web having an average fiber diameter of 2.5 dtex.
Then, the obtained filament web was flat-rolled and embossed-rolled at a temperature of 135° C. and a pressure of 60 kg/cm (pattern specifications: circle diameter 1.00 mm, staggered arrangement, horizontal pitch 4.4 mm, vertical pitch 4.4 mm, The fibers were partially adhered to each other by passing the fibers through a pressure-bonding area ratio of 7.9%) to obtain a filament nonwoven fabric (3) having a basis weight of 15 g/m ² and a number of crimps of 28/inch.

<Production of nonwoven fabric (4)>
A polypropylene (PP) resin with an MFR of 55 g/10 minutes (measured at a temperature of 230° C. and a load of 2.16 kg according to JIS-K7210) is used as the first component, and a melt index (MI) of 26 g/10 minutes (JIS-K7210 Measured at a temperature of 190 ° C and a load of 2.16 kg) as the second component, the discharge amount of the first component is 0.54 g / min hole, and the discharge amount of the second component is A fiber having a total discharge rate of 0.8 g/min.hole at 0.26 g/min.hole and a ratio of the first component to the second component of about 2/1 was extruded at a spinning temperature of 220°C by a spunbond method. Using a high-speed airflow drawing device with an air jet, this filament group was extruded toward a moving collecting surface to prepare an eccentric sheath-core type composite filament web having an average fiber diameter of 2.0 dtex.
Next, using the same flat roll/embossing roll as used in the production of the nonwoven fabric (3), the obtained filament web was partially pressed against each other under the conditions of a top and bottom temperature of 135°C and a pressure of 60 kg/cm. A long fiber nonwoven fabric (4) was obtained by adjusting the line speed so that the target basis weight was 15 g/m ² .

<Production of nonwoven fabric (5)>
The first component is a polypropylene (PP) resin with an MFR of 55 g/10 minutes (according to JIS-K7210, measured at a temperature of 230 ° C and a load of 2.16 kg), and an MI of 26 g/10 minutes (according to JIS-K7210, temperature (measured at 190 ° C. and a load of 2.16 kg) is used as the second component, the discharge amount of the first component is 0.4 g / min hole, the discharge amount of the second component is 0.4 g / A fiber having a total discharge amount of 0.8 g/min.hole and a ratio of the first component to the second component of 1/1 is extruded by a spunbond method at a spinning temperature of 220 ° C., and this filament group is formed. An eccentric sheath-core type composite filament web having an average fiber diameter of 2.3 dtex was prepared by extruding toward a moving collecting surface using a high-speed airflow drawing device with an air jet.
Next, the obtained eccentric sheath-core type composite long fiber nonwoven web was rolled at 100° C. with a flat roll and an embossed roll (pattern specifications: circle diameter 1.00 mm, staggered arrangement, horizontal pitch 4.4 mm, vertical pitch 4.4 mm, The fibers are temporarily bonded together by passing them through a crimping area ratio of 7.9%), and then the fibers are bonded together by hot air with a hot air temperature of 142 ° C. and a hot air velocity of 0.7 ^m / s. A composite long fiber nonwoven fabric (5) with a shrinkage number of 17 pieces/inch was obtained.

<Production of nonwoven fabric (6)>
Using the same polymer as used in the production of nonwoven fabric (5), the discharge amount of the first component (polypropylene) is 0.40 g/min.hole, and the discharge amount of the second component (polyethylene) is 0.40 g. A fiber having a total discharge rate of 0.8 g/min·hole and a ratio of the first component to the second component of 1:1 was extruded at a spinning temperature of 220° C. by a spunbond method. The extruded filaments are stretched in the pulling zone using the suction force of the moving collection surface, passed through a diffuser and deposited on the moving collection surface to form a side-by-side type composite continuous fiber web having an average fiber diameter of 3.0 dtex. was prepared. The obtained side-by-side type conjugate long-fiber web was bonded with hot air at a hot-air temperature of 142° C. and a hot-air speed of 0.7 m/s to form a conjugate long-fiber nonwoven fabric having a basis weight of 15 g/m ² and a number of crimps of 15/inch ( 6) was obtained.

<Production of nonwoven fabric (7)>
The first component is a polypropylene (PP) resin with an MFR of 36 g/10 minutes (according to JIS-K7210, measured at a temperature of 230 ° C and a load of 2.16 kg), and an MI of 17 g/10 minutes (according to JIS-K7210, temperature 190 ° C., a load of 2.16 kg) linear low-density linear polyethylene (LLDPE) resin is used as the second component, the discharge amount of the first component is 0.50 g / min.hole, the discharge amount of the second component is 0.25 g/min.hole, the total discharge rate is 0.75 g/min.hole, and the ratio of the first component to the second component is 2/1. Using a high-speed airflow drawing device with an air jet, this filament group was extruded toward a moving collecting surface to prepare an eccentric sheath-core type composite filament web having an average fiber diameter of 2.8 dtex.
Then, the fibers were bonded together by hot air at a hot air temperature of 120° C. and a hot air velocity of 1.0 m/s to obtain a composite filament nonwoven fabric (7) having a basis weight of 20 g/m ² and a number of crimps of 25/inch.

<Production of nonwoven fabric (8)>
A polyethylene terephthalate (PET) resin with a solution viscosity of ηsp/c of 0.75 is used as the first component, and MI is 26 g/10 min (according to JIS-K7210, measured at a temperature of 190 ° C. and a load of 2.16 kg). ) The resin is used as the second component, the discharge amount of the first component is 0.50 g/min.hole, the discharge amount of the second component is 0.25 g/min.hole, and the total discharge amount is 0.75 g/min.hole A fiber having a ratio of the first component to the second component of 2:1 was extruded at a spinning temperature of 220°C by a spunbond method. The extruded filaments are stretched in the traction zone using the suction force of the moving collection surface, then passed through a diffuser and deposited on the moving collection surface to form an eccentric sheath-core composite with an average fiber diameter of 4.0 dtex. A long fiber web was prepared. The obtained eccentric sheath-core type conjugate long fiber web was bonded with hot air at a hot air temperature of 130° C. and a hot air velocity of 0.7 m/s to obtain a composite length with a basis weight of 30 g/m ² and a number of crimps of 13/inch. A fibrous nonwoven fabric (8) was obtained.

<Component (A)>
Component A-1: Propylene glycol manufactured by ADEKA Corporation was used.
Component A-2: Dipropylene glycol manufactured by ADEKA Corporation was used.

<Component (B)>
Component B-1: Polyoxyalkylene glycol was obtained by adding 30 mol of propylene oxide and then 8 mol of ethylene oxide to propylene glycol according to a conventional method. Then, 1 mol of this polyoxyalkylene glycol was reacted with 1.5 mol of lauric acid to obtain Component B-1. Component B-1 is represented by general formula (2), wherein n is 0, R ¹ and R ³ are alkenoyl groups having 11 carbon atoms, and (A ² O) ₁ is a total of 31 mol of propylene oxide at both ends. A compound in which 8 mol of ethylene oxide is added (l is 39), and in general formula (2), n is 0 and either one of R ¹ and R ³ is an alkenoyl group having 11 carbon atoms; , (A ² O) _l is a group (l is 39) in which a total of 8 moles of ethylene oxide is added to both ends of 31 moles of propylene oxide.

Component B-2: Polyoxyalkylene glycol was obtained by adding 50 mol of propylene oxide and then 15 mol of ethylene oxide to propylene glycol in accordance with a conventional method. Then, 1 mol of this polyoxyalkylene glycol was reacted with 1.8 mol of stearic acid to obtain Component B-2. Component B-2 is represented by general formula (2), wherein n is 0, R ¹ and R ³ are alkenoyl groups having 17 carbon atoms, and (A ² O) ₁ is a total of 51 mol of propylene oxide at both ends. 15 moles of ethylene oxide-added group (l is 66), and in general formula (2), n is 0 and either one of R ¹ and R ³ is an alkenoyl group having 17 carbon atoms; , (A ² O) _l is a group (1 is 66) in which a total of 15 moles of ethylene oxide is added to both ends of 51 moles of propylene oxide.

Component B-3: Polyoxyalkylene glycol was obtained by adding 30 mol of propylene oxide and then 8 mol of ethylene oxide to propylene glycol according to a conventional method. Then, 3 mol of this polyoxyalkylene glycol and 2 mol of adipic acid were reacted. Then, this reactant was reacted with 1 mol of lauric acid to obtain Component B-3.
In component B-3, in the general formula (2), either one of R ¹ and R ³ is an alkenoyl group having 11 carbon atoms, and (A ² O) ₁ is 8 mol in total at both ends of 31 mol of propylene oxide. is a group to which ethylene oxide is added (l is 39), R ² is an alkylene group having 4 carbon atoms, and (A ³ O) _m is a total of 8 mol of ethylene oxide added to both ends of 31 mol of propylene oxide. (m is 39) and n is 2.

Component B-4: Polyoxyalkylene glycol was obtained by adding 30 mol of propylene oxide and then 8 mol of ethylene oxide to propylene glycol in accordance with a conventional method. Then, 5 mol of this polyoxyalkylene glycol and 4 mol of adipic acid were reacted to obtain Component B-4. Component ^{B - 4} is a group ( _l is 39), R ² is an alkylene group having 4 carbon atoms, and (A ³ O) _m is a group obtained by adding a total of 8 mol of ethylene oxide to both ends of 31 mol of propylene oxide (m is 39). , n is 4.

Component B-5: Component B-5 was obtained by adding 24 mol of propylene oxide to lauryl alcohol according to a conventional method.
Component B-5 is represented by general formula (2), wherein n is 0, R ¹ and R ³ are alkyl groups having 12 carbon atoms, and (A ² O) _l is a group containing 24 moles of propylene oxide (l is 24).

<Component (C)>
KF-6013 (manufactured by Shin-Etsu Chemical Co., Ltd., HLB=10, viscosity 400 cSt) was used as the polyether-modified silicone.

Concentrated glycerin for cosmetics manufactured by Miyoshi Oil Co., Ltd. was used as glycerin.

<Polyether>
Polypropylene glycol having an average degree of polymerization of 85 was obtained by addition polymerization of propylene oxide to water. Next, ethylene oxide was added to the polypropylene glycol so as to have an average degree of polymerization of 25 to obtain a block polyether compound of (propylene oxide) 85.(ethylene oxide) 25 having an average molecular weight of about 6,000.

<Glycerin condensate>
As the glycerin condensate, hexaglycerin monostearate (manufactured by Sakamoto Yakuhin Kogyo Co., Ltd., trade name: SY Glystar MS-5S) was used.

<Polyoxyalkylene Castor Oil Ether>
Polyoxyethylene (20) hydrogenated castor oil (manufactured by Nikko Chemical Co., Ltd., trade name: NIKKOL HCO-20) was used as the polyoxyalkylene castor oil ether.

[Example 1]
Component A-1: 25 parts by mass as component (A), component B-1: 55 parts by mass as component (B), and component (C): 20 parts by mass are uniformly mixed at 30 ° C. The fiber of Example 1 A processing agent (1) was obtained. The blending ratio of each component is shown in Table 1 below.

[Examples 2 to 7, 9, Reference Examples 8, 10, Comparative Examples 1 to 7]
Examples 2 to 7, 9, Fiber finishing agents (2) to (10) of Reference Examples 8 and 10 and fiber finishing agents (Comparative 1) to (Comparative 7) of Comparative Examples 1 to 7 were obtained. The blending ratio of each component is shown in Table 1 below.

[Example 11]
A 3% by weight aqueous solution of the fiber processing agent (1) of Example 1 was applied to the nonwoven fabric (1) at a liquid temperature of 20° C., and the coating amount was 10% by weight by the rotor dampening method. It was applied to a non-woven fabric, passed through an air-through dryer at 125°C, dried, and wound up. The diameter of the rotors of the rotor dampening apparatus used was 80 mm, and the rotors were arranged at intervals of 115 mm in the CD direction so that the distance between the center of the rotor and the nonwoven fabric to be applied was 180 mm. In addition, the rotor rotation speed was adjusted so that the spray particle size of the sprayed fiber processing agent was 35 μm. Various measurement results of the obtained nonwoven fabric are shown in Table 2-1 below.

[Example 12]
The fiber processing agent (2) of Example 2 was added to the nonwoven fabric (1) in the same manner as in Example 11. Various measurement results of the obtained nonwoven fabric are shown in Table 2-1 below.

[Example 13]
The fiber processing agent (3) of Example 3 was added to the nonwoven fabric (1) in the same manner as in Example 11. Various measurement results of the obtained nonwoven fabric are shown in Table 2-1 below.

[Example 14]
A 5% by weight aqueous solution of the fiber processing agent (2) of Example 2 was applied to the nonwoven fabric (1) at a liquid temperature of 20° C., except that the coating amount was 10% by weight. It was applied to the nonwoven fabric in the same manner. Various measurement results of the obtained nonwoven fabric are shown in Table 2-1 below.

[Example 15]
A 3.4% by weight aqueous solution of the fiber processing agent (4) of Example 4 was applied to the nonwoven fabric (1) at a liquid temperature of 20° C., and a slanting pattern of 120 mesh was applied so that the coating amount was 30% by weight. It was applied using a gravure roll with a cell volume of 22 cm ³ /m ² , then dried through a cylinder dryer at 120° C. and wound up. Various measurement results of the obtained nonwoven fabric are shown in Table 2-1 below.

[Example 16]
A 10% by weight aqueous solution of the fiber processing agent (5) of Example 5 was applied to the nonwoven fabric (1) at a liquid temperature of 20° C., except that the coating amount was 10% by weight. It was applied to the nonwoven fabric in the same manner. Various measurement results of the obtained nonwoven fabric are shown in Table 2-1 below.

[Example 17]
A nonwoven fabric was obtained in the same manner as in the production (1) of the nonwoven fabric, except that the line speed was adjusted so that the basis weight was 8 g/m ² . The obtained nonwoven fabric was subjected to corona treatment so that the wet tension of the nonwoven fabric was 35 to 39 mN/m, and then a 0.34% by weight aqueous solution of the fiber processing agent (4) of Example 4 was added at a liquid temperature of 20 ° C. It was applied to the nonwoven fabric in the same manner as in Example 15, except for the preparation. Various measurement results of the obtained nonwoven fabric are shown in Table 2-1 below.

[Example 18]
A nonwoven fabric was obtained in the same manner as in the production (1) of the nonwoven fabric, except that the line speed was adjusted so that the basis weight was 15 g/m ² . A 1.67% by weight aqueous solution of the fiber processing agent (4) of Example 4 was applied to the obtained nonwoven fabric in the same manner as in Example 15, except that the liquid temperature was adjusted to 20°C. Various measurement results of the obtained nonwoven fabric are shown in Table 2-1 below.

[Example 19]
The nonwoven fabric (2) was coated with a 10% by weight aqueous solution of the fiber processing agent (4) of Example 4 at a liquid temperature of 20° C., except that the coating amount was 10% by weight. It was applied to the nonwoven fabric in the same manner. Various measurement results of the obtained nonwoven fabric are shown in Table 2-1 below.

[Example 20]
A nonwoven fabric was produced in the same manner as in Example 19, except that the fiber processing agent (6) was used. Various measurement results of the obtained nonwoven fabric are shown in Table 2-1 below.

[Example 21]
A nonwoven fabric was obtained in the same manner as in the production (2) of the nonwoven fabric, except that the line speed was adjusted so that the basis weight was 18 g/m ² . The resulting nonwoven fabric was applied to the nonwoven fabric in the same manner as in Example 15, except that a 1.0% by weight aqueous solution of the fiber processing agent (7) of Example 7 was adjusted at a liquid temperature of 20°C. Various measurement results of the obtained nonwoven fabric are shown in Table 2-1 below.

[ Reference Example 22]
A nonwoven fabric was obtained in the same manner as in the production (1) of the nonwoven fabric, except that the line speed was adjusted so that the basis weight was 15 g/m ² . A nonwoven fabric was produced in the same manner as in Example 21, except that the fiber processing agent (8) was used. Various measurement results of the obtained nonwoven fabric are shown in Table 2-1 below.

[Example 23]
A 0.67% by weight aqueous solution of the fiber processing agent (7) was applied to the nonwoven fabric (3) in the same manner as in Example 15, except that the solution temperature was 20°C. Various measurement results of the obtained nonwoven fabric are shown in Table 2-1 below.

[Example 24]
A nonwoven fabric was produced in the same manner as in Example 23, except that the nonwoven fabric (4) was used. Various measurement results of the obtained nonwoven fabric are shown in Table 2-1 below.

[Example 25]
A nonwoven fabric was prepared in the same manner as in Example 11, except that a 2% by weight aqueous solution of the fiber processing agent (7) was applied to the nonwoven fabric (5) at a liquid temperature of 20° C. so that the coating amount was 10% by weight. made. Various measurement results of the obtained nonwoven fabric are shown in Table 2-1 below.

[Example 26]
A fibrous nonwoven fabric was produced in the same manner as in Example 25, except that the nonwoven fabric (6) was used. Various measurement results of the obtained nonwoven fabric are shown in Table 2-1 below.

[Example 27]
A nonwoven fabric was prepared in the same manner as in Example 11, except that a 10% by weight aqueous solution of the fiber processing agent (4) was applied to the nonwoven fabric (7) at a liquid temperature of 20° C. so that the coating amount was 5% by weight. made. Various measurement results of the obtained nonwoven fabric are shown in Table 2-2 below.

[Example 28]
A nonwoven fabric was prepared in the same manner as in Example 11, except that a 6% by weight aqueous solution of the fiber processing agent (4) was prepared on the nonwoven fabric (8) at a liquid temperature of 20° C. so that the coating amount was 5% by weight. made. Various measurement results of the obtained nonwoven fabric are shown in Table 2-2 below.

[Example 29]
A 0.67% by weight aqueous solution of the fiber processing agent (4) was prepared at a liquid temperature of 20° C. and applied to the nonwoven fabric (5) using a kiss roll (φ400 mm) so that the coating amount was 30% by weight. , through a cylinder dryer at 130° C. and wound up. Various measurement results of the obtained nonwoven fabric are shown in Table 2-2 below.

[Example 30]
Nonwoven fabric in the same manner as in Example 11, except that a 5% by weight aqueous solution of the fiber processing agent (9) was applied to the nonwoven fabric (1) at a liquid temperature of 20 ° C. so that the coating amount was 10% by weight. was made. Various measurement results of the obtained nonwoven fabric are shown in Table 2-2 below.

[ Reference Example 31]
A 3% by weight aqueous solution of the fiber processing agent (10) of Reference Example 10 was applied to the nonwoven fabric (1) at a liquid temperature of 20° C., except that the coating amount was 10% by weight. A nonwoven fabric was produced in the same manner. Various measurement results of the obtained nonwoven fabric are shown in Table 2-2 below.

[Comparative Example 11]
The fiber processing agent of Comparative Example 1 (Comparative (1)) was applied to the nonwoven fabric (1) in the same manner as in Example 14. Various measurement results of the obtained nonwoven fabric are shown in Table 2-2 below.

[Comparative Example 12]
A nonwoven fabric was obtained in the same manner as in Comparative Example 11, except that the fiber processing agent of Comparative Example 2 (Comparative (2)) was used. Various measurement results of the obtained nonwoven fabric are shown in Table 2-2 below.

[Comparative Example 13]
A nonwoven fabric was obtained in the same manner as in Comparative Example 11, except that the fiber processing agent of Comparative Example 3 (Comparative (3)) was used. Various measurement results of the obtained nonwoven fabric are shown in Table 2-2 below.

[Comparative Example 14]
A 1.67% by weight aqueous solution of the fiber processing agent (comparative (4)) of Comparative Example 4 was applied to the nonwoven fabric (1) in the same manner as in Example 15, except that the liquid temperature was 20°C. Various measurement results of the obtained nonwoven fabric are shown in Table 2-2 below.

[Comparative Example 15]
A 1.0% by weight aqueous solution of the fiber processing agent of Comparative Example 5 (Comparative (5)) was applied to the nonwoven fabric (1) in the same manner as in Example 15, except that the liquid temperature was 20°C. Various measurement results of the obtained nonwoven fabric are shown in Table 2-2 below.

[Comparative Example 16]
A 1.67% by weight aqueous solution of the fiber processing agent of Comparative Example 6 (Comparative (6)) was applied to the nonwoven fabric (1) in the same manner as in Example 15, except that the liquid temperature was 20°C. Various measurement results of the obtained nonwoven fabric are shown in Table 2-2 below.

[Comparative Example 17]
A nonwoven fabric was produced in the same manner as in Example 11, except that the fiber processing agent of Comparative Example 7 (Comparative (7)) was used. Various measurement results of the obtained nonwoven fabric are shown in Table 2-2 below.

Since the nonwoven fabric coated with the fiber processing agent according to the present invention has excellent initial water permeability, rewetting property, and repeated water permeability, it can be used as a top sheet or second sheet for sanitary materials such as sanitary napkins, incontinence pads, and disposable diapers. Alternatively, for example, masks, body warmers, tape bases, patch bases, emergency bandages, packaging materials, wipe products, medical gowns, bandages, clothing, skin care sheets, etc. available for

Claims (8)

The following general formula (1):
HO—(A ¹ O) _p —H General formula (1)
{In the formula, A ¹ is an alkylene group having 2 to 4 carbon atoms, and p is an integer of 1 to 3. } and the following general formula (2) different from the component (A):
R ¹ —O—(A ² O) ₁ —{C(O)R ² C(O)—O—(A ³ O) _m } _n —R ³ General formula (2)
{In the formula, R ¹ and R ³ are each independently a hydrogen atom, an alkyl group having 1 to 24 carbon atoms, an alkenyl group having 2 to 24 carbon atoms, an alkanoyl group having 2 to 24 carbon atoms, or an alkanoyl group having 2 to 24 carbon atoms. where only one of R ¹ and R ³ is non-hydrogen is a mono-form, and where both R ¹ and R ³ are non-hydrogen is a di-form, the mono-form and the ratio of the di-form is mono-form: di-form = 10:0 to 1:9, and R ² is an alkylene group having 1 to 12 carbon atoms, an alkenylene group having 2 to 12 carbon atoms or an alkenylene group having 6 to 12 carbon atoms. is an arylene group, A ² and A ³ are each independently an alkylene group having 2 or 3 carbon atoms, l is an integer of 10 to 200, m is an integer of 39 , and n is an integer of 0 or 1-2 . provided that either one of R ¹ and R ³ is an alkyl group having 1 to 24 carbon atoms, an alkenyl group having 2 to 24 carbon atoms, an alkanoyl group having 2 to 24 carbon atoms, or an alkenoyl group having 2 to 24 carbon atoms; and l+n is 1 or more, and not all of A ² and A ³ are alkylene groups having 2 carbon atoms. } component (B) represented by; and component (C) which is a polyether-modified silicone;
and the component (C) is 10% by mass to 30% by mass with respect to the total amount of the component (A) and the component (B). A liquid-permeable nonwoven fabric, wherein the amount of the fiber processing agent according to claim 1 is 0.1 to 1.5% by weight. 3. The liquid-permeable nonwoven fabric according to claim 2, wherein the liquid-permeable nonwoven fabric is a nonwoven fabric made of thermoplastic fibers. 4. The liquid-permeable nonwoven fabric according to claim 2, wherein the nonwoven fabric is made of fibers having a fineness of 0.45 to 5.0 dtex. The liquid-permeable nonwoven fabric according to any one of claims 2 to 4, wherein the nonwoven fabric is a long-fiber nonwoven fabric. The liquid-permeable nonwoven fabric according to any one of claims 2 to 5, wherein the repeated water permeability of the liquid-permeable nonwoven fabric is 70% or more at the fourth time. The liquid-permeable nonwoven fabric according to any one of claims 2 to 6, wherein the liquid-permeable nonwoven fabric has a rewetting property of 0.5 g or less. A sanitary material using the liquid-permeable nonwoven fabric according to any one of claims 2 to 7.