JP6433837B2 - Deodorant fiber - Google Patents

Description

  The present invention relates to a deodorizing fiber.

  Recently, functional fibers imparted with various functions have been developed, and as one of such functional fibers, deodorant fibers imparted with a deodorant function have been proposed (for example, Patent Documents 1 to 3). 4).

  However, in the conventional deodorizing fiber, the component for imparting deodorizing performance is easily detached from the fiber, and it cannot be said that the deodorizing performance is sufficiently high. For this reason, the deodorizing fiber which the component for providing deodorizing performance cannot express easily from a fiber, and can express the excellent deodorizing performance is calculated | required.

Japanese Patent Publication No.8-13905 Japanese Patent No. 3517045 Japanese Patent No. 3279120 Japanese Patent No. 3304067

  The subject of this invention is providing the deodorizing fiber which can express the deodorizing performance which the component for providing deodorizing performance is hard to detach | leave from a fiber, and was excellent.

The deodorant fiber of the present invention is
A deodorizing fiber containing a (meth) acrylic acid (salt) copolymer and cellulose,
The (meth) acrylic acid (salt) copolymer comprises a structural unit (A) derived from a monoethylenically unsaturated monocarboxylic acid (salt) monomer (a) and a monoethylenically unsaturated dicarboxylic acid (salt). Or at least one selected from the structural unit (B) derived from the monomer (b) which is an anhydride thereof and the structural unit (C) derived from the ether bond-containing hydrophobic monomer (c). It is a polymer.

  In preferable embodiment, the said structural unit (A), the said structural unit (B), and the said structural unit with respect to the sum total of the structural unit derived from all the monomers in the said (meth) acrylic acid (salt) type | system | group copolymer. The total content of (C) is 90 mol% to 100 mol%.

  In preferable embodiment, the weight average molecular weights of the said (meth) acrylic acid (salt) type | system | group copolymer are 1000-500000.

  In a preferred embodiment, the ether bond-containing hydrophobic monomer (c) is 1-allyloxy-3-butoxypropan-2-ol.

  ADVANTAGE OF THE INVENTION According to this invention, the deodorizing fiber which can express the deodorizing performance which the component for providing deodorizing performance cannot express easily from a fiber, and was excellent can be provided.

  In the present specification, the expression “acid (salt)” means an acid and / or an acid salt. The “salt” is preferably an alkali metal salt such as sodium salt or potassium salt; an alkaline earth metal salt such as calcium salt or magnesium salt; an ammonium salt; an organic amine salt such as monoethanolamine salt or triethanolamine salt. And so on. “Salt” may be only one kind or a mixture of two or more kinds. The “salt” is more preferably an alkali metal salt such as a sodium salt or a potassium salt, and still more preferably a sodium salt.

  In the present specification, the expression “(meth) acryl” means “acryl and / or methacryl”, and the expression “(meth) acrylate” means “acrylate and / or methacrylate”. Means “allyl and / or methallyl”, and “(meth) acrolein” means “acrolein and / or methacrole”. It means "rain".

  The deodorizing fiber of the present invention contains a (meth) acrylic acid (salt) copolymer and cellulose. The deodorant fiber of this invention may contain arbitrary appropriate other components in the range which does not impair the effect of this invention. The deodorant fiber of the present invention is preferably a cellulose fiber in which a (meth) acrylic acid (salt) copolymer is contained in cellulose.

  In the deodorizing fiber of the present invention, the content of the (meth) acrylic acid (salt) copolymer is preferably 0.1 parts by mass to 50 parts by mass, more preferably 100 parts by mass of cellulose. 0.5 parts by mass to 40 parts by mass, more preferably 1 part by mass to 30 parts by mass, particularly preferably 2 parts by mass to 20 parts by mass, and most preferably 4 parts by mass to 10 parts by mass. . When there is too much content of a (meth) acrylic acid (salt) type-system copolymer, there exists a possibility that fiber strength may fall. If the content of the (meth) acrylic acid (salt) copolymer is too small, there is a possibility that sufficient deodorizing performance cannot be expressed.

  The deodorant fiber of the present invention has a fineness of preferably 0.3 dtex (decitex) to 8.0 dtex, more preferably 0.6 dtex to 6.0 dtex, and still more preferably 0.7 dtex to 3.6 dtex. is there. If the fineness of the deodorant fiber of the present invention is less than 0.3 dtex, the single fiber may be broken during stretching. If the fineness of the deodorant fiber of the present invention exceeds 8.0 dtex, the fiber regeneration state tends to be poor, and the hue of the fiber may be deteriorated.

  The deodorizing fiber of the present invention can be preferably provided in the form of long fibers or short fibers. Examples of the long fiber include tow, filament, and non-woven fabric. Examples of the short fiber include raw paper for wet papermaking, raw cotton for airlaid nonwoven fabric, and raw cotton for card.

  The deodorant fiber of this invention can form a fiber structure, for example. Examples of the fiber structure include tow, filament, spun yarn, batting (padded cotton), paper, nonwoven fabric, woven fabric, knitted fabric, and the like.

  The deodorant fiber of the present invention can be preferably produced by spinning a viscose solution for spinning prepared by mixing a (meth) acrylic acid (salt) copolymer with a viscose stock solution containing cellulose. The obtained viscose rayon yarn may be subjected to pH adjustment treatment as necessary.

  Any appropriate viscose stock solution may be employed as the raw material viscose as long as the effects of the present invention are not impaired. As such a viscose stock solution, preferably 3% to 20% by mass (preferably 7% to 10% by mass) of cellulose and 1% to 15% by mass (preferably 5% by mass) of sodium hydroxide. To 8% by mass) and viscose stock solution containing 0.1% to 10% by mass (preferably 2% to 3.5% by mass) of carbon disulfide. At this time, additives such as ethylenediaminetetraacetic acid (EDTA) and titanium dioxide can be used as necessary. The temperature of the raw material viscose is preferably maintained at 18 to 23 ° C.

  Any appropriate spinning bath can be adopted as the spinning bath (Mueller bath) as long as the effects of the present invention are not impaired. As such a spinning bath, a strong acid bath containing 95 to 130 g / L of sulfuric acid, 10 to 17 g / L of zinc sulfate, and 290 to 370 g / L of sodium sulfate (sodium salt) is preferable.

  The deodorant fiber of this invention can be manufactured using arbitrary appropriate spinning nozzles in the range which does not impair the effect of this invention. For example, it can be manufactured using a normal circular nozzle. Examples of the spinning nozzle include a circular nozzle having a diameter of 0.05 mm to 0.12 mm and a number of holes of 1000 to 20000, depending on the target production amount. Alternatively, a nozzle having an irregular cross section may be used. For example, if spinning is performed using a Y type nozzle, a fiber having a large surface area and particularly an excellent initial water absorption rate can be obtained.

  The deodorant fiber of the present invention can be produced by using the spinning nozzle as described above to extrude the spinning viscose stock solution into a spinning bath, spin it, and coagulate it. The spinning speed is preferably 30 m / min to 80 m / min. The stretch ratio is preferably 39% to 55%. Here, the stretching ratio indicates how much the sliver speed after stretching is increased when the sliver speed before stretching is 100. In terms of magnification, it is 1 before stretching and 1.39 to 1.55 times after stretching.

  In order to obtain the deodorant fiber of the present invention, the rayon fiber yarn thus obtained is preferably cut into a predetermined length and subjected to a scouring treatment. The scouring step is preferably performed in the order of hot water treatment, hydrosulfurization treatment, bleaching, pickling, and oil application. Then, if necessary, excess oil agent and water | moisture content are removed from a fiber by methods, such as a compression roller and a vacuum suction, and it can dry-process, and can obtain the deodorizing fiber of this invention.

  The deodorant fiber of the present invention contains a (meth) acrylic acid (salt) copolymer.

  The (meth) acrylic acid (salt) copolymer comprises a structural unit (A) derived from a monoethylenically unsaturated monocarboxylic acid (salt) monomer (a) and a monoethylenically unsaturated dicarboxylic acid (salt). Or at least one selected from the structural unit (B) derived from the monomer (b), which is an anhydride thereof, and the structural unit (C) derived from the ether bond-containing hydrophobic monomer (c). It is a coalescence. By including such a (meth) acrylic acid (salt) -based copolymer, the deodorizing fiber of the present invention has an excellent deodorizing performance in which the component for imparting the deodorizing performance is not easily detached from the fiber. It can be expressed.

  The (meth) acrylic acid (salt) copolymer is preferably a structural unit derived from a monoethylenically unsaturated monocarboxylic acid (salt) monomer (a) in that the effects of the present invention can be further exhibited. (A) and the structural unit (B) derived from the monomer (b) which is a monoethylenically unsaturated dicarboxylic acid (salt) or its anhydride are essential.

“Monomer-derived structural unit” means a structural unit in which an unsaturated double bond involved in a polymerization reaction in a monomer is converted to a single bond by a polymerization reaction. Specifically, a monomer when expressed in ^{"R 1 R 2 C = CR 3} R 4 " and, in the copolymer - it means a structural unit represented by ^{"-R 1 R 2 C-CR 3} R 4 ". For example, a structural unit derived from acrylic acid is represented by “—CH ₂ —CH (COOH) —”, and a structural unit derived from maleic acid is represented by “—CH (COOH) —CH (COOH) —”. .

  The monoethylenically unsaturated monocarboxylic acid (salt) monomer (a) is preferably a monoethylenically unsaturated monocarboxylic acid (salt) monomer having 3 to 8 carbon atoms. Examples of such monoethylenically unsaturated monocarboxylic acid (salt) monomer (a) include acrylic acid (salt), methacrylic acid (salt), crotonic acid (salt), isocrotonic acid (salt), α -Hydroxyacrylic acid (salt) etc. are mentioned. The monoethylenically unsaturated monocarboxylic acid (salt) monomer (a) may be a single type or a mixture of two or more types. The monoethylenically unsaturated monocarboxylic acid (salt) monomer (a) is preferably acrylic acid (salt) or methacrylic acid (salt), more preferably acrylic acid (salt).

  The monomer (b) which is a monoethylenically unsaturated dicarboxylic acid (salt) or its anhydride is preferably a monoethylenically unsaturated dicarboxylic acid (salt) having 4 to 6 carbon atoms or its anhydride. is there. Examples of such a monomer (b) that is a monoethylenically unsaturated dicarboxylic acid (salt) or an anhydride thereof include maleic acid (salt), itaconic acid (salt), mesaconic acid (salt), and fumaric acid. (Salt), citraconic acid (salt), and those which may have an anhydrous form include the anhydride. The monomer (b), which is a monoethylenically unsaturated dicarboxylic acid (salt) or its anhydride, may be only one kind or a mixture of two or more kinds. The monomer (b) which is a monoethylenically unsaturated dicarboxylic acid (salt) or its anhydride is preferably maleic acid (salt) or maleic anhydride (salt).

The ether bond-containing hydrophobic monomer (c) is preferably represented by the general formula (1). The ether bond-containing hydrophobic monomer (c) may be a single type or a mixture of two or more types.

In general formula (1), R ¹ is a hydrogen atom or a methyl group.

In the general formula (1), R ² is an alkylene group having 1 to 10 carbon atoms, preferably an alkylene group having 1 to 8 carbon atoms, more preferably an alkylene group having 1 to 5 carbon atoms, preferably an alkylene group having 1 to 3 carbon atoms, particularly preferably an alkylene group having 1 to 2 carbon atoms (i.e., -CH ₂ - or _{-CH 2} CH 2 -) a.

In the general formula (1), R ³ is an alkylene group having 1 to 10 carbon atoms, preferably an alkylene group having 1 to 8 carbon atoms, more preferably an alkylene group having 1 to 5 carbon atoms, more An alkylene group having 1 to 3 carbon atoms is preferable, an alkylene group having 1 to 2 carbon atoms is particularly preferable, and an alkylene group having 1 carbon atom (that is, —CH ₂ —) is most preferable.

In general formula (1), R ⁴ is a hydrogen atom or a hydroxyl group.

In the general formula (1), ^{R 5} is -OR ⁶ group or ^{R 6, R 6} is an alkyl group having 1 to 20 carbon atoms, preferably an alkyl group having 1 to 18 carbon atoms, more preferably Is an alkyl group having 1 to 13 carbon atoms, more preferably an alkyl group having 1 to 8 carbon atoms, and particularly preferably an alkyl group having 1 to 5 carbon atoms.

  The ether bond-containing hydrophobic monomer (c) is more preferably 1-allyloxy-3-butoxypropan-2-ol represented by the chemical formula (2) or hexene oxide of isoprenol represented by the chemical formula (3) The adduct is at least one selected from allyl butyl ether represented by the chemical formula (4).

  The ether bond-containing hydrophobic monomer (c) is more preferably 1-allyloxy-3-butoxypropan-2-ol represented by the chemical formula (2) in that the effects of the present invention can be further exhibited. It is.

  The total content ratio of the structural unit (A), the structural unit (B), and the structural unit (C) with respect to the total of the structural units derived from all monomers in the (meth) acrylic acid (salt) copolymer is as follows: Preferably, it is 90 mol% to 100 mol%, more preferably 95 mol% to 100 mol%, still more preferably 98 mol% to 100 mol%, and particularly preferably substantially 100 mol% (ie, , (Meth) acrylic acid (salt) -based copolymer comprises a monoethylenically unsaturated monocarboxylic acid (salt) monomer (a) -derived structural unit (A) and a monoethylenically unsaturated dicarboxylic acid (salt). Or at least one selected from the structural unit (B) derived from the monomer (b) which is an anhydride thereof and the structural unit (C) derived from the ether bond-containing hydrophobic monomer (c)) It is.

  The content ratio of the structural unit (A) with respect to the total of structural units derived from all monomers in the (meth) acrylic acid (salt) copolymer is preferably 0.1 mol% to 99 mol%, More preferably, it is 1 mol%-98 mol%, More preferably, it is 10 mol%-97 mol%, More preferably, it is 20 mol%-96 mol%, More preferably, it is 30 mol%-95 mol% Particularly preferably 40 to 93 mol%, most preferably 50 to 90 mol%. Deodorization of the present invention by adjusting the content ratio of the structural unit (A) with respect to the total of structural units derived from all monomers in the (meth) acrylic acid (salt) copolymer within the above range. In the fiber, a component for imparting deodorant performance is less likely to be detached from the fiber, and more excellent deodorant performance can be exhibited.

  When the (meth) acrylic acid (salt) copolymer has a structural unit (B) derived from a monomer (b) that is a monoethylenically unsaturated dicarboxylic acid (salt) or its anhydride, (meth) acrylic The content ratio of the structural unit (B) to the total of structural units derived from all monomers in the acid (salt) copolymer is preferably 0.1 mol% to 99 mol%, more preferably 1 Mol% to 95 mol%, more preferably 5 mol% to 90 mol%, more preferably 10 mol% to 80 mol%, still more preferably 15 mol% to 70 mol%, and particularly preferably Is 20 mol% to 60 mol%, most preferably 30 mol% to 50 mol%. By adjusting the content ratio of the structural unit (B) with respect to the total of structural units derived from all the monomers in the (meth) acrylic acid (salt) -based copolymer within the above range, the deodorization of the present invention. In the fiber, a component for imparting deodorant performance is less likely to be detached from the fiber, and more excellent deodorant performance can be exhibited.

  When the (meth) acrylic acid (salt) copolymer has a structural unit (C) derived from the ether bond-containing hydrophobic monomer (c), all of the (meth) acrylic acid (salt) copolymer in the copolymer The content ratio of the structural unit (C) with respect to the total of the structural units derived from the monomer is preferably 0.1 mol% to 50 mol%, more preferably 0.3 mol% to 40 mol%, More preferably, it is 0.5 mol%-30 mol%, More preferably, it is 0.8 mol%-20 mol%, More preferably, it is 1 mol%-10 mol%, Most preferably, it is 2 mol%- 8 mol%, and most preferably 3 mol% to 7 mol%. By adjusting the content ratio of the structural unit (C) with respect to the total of structural units derived from all monomers in the (meth) acrylic acid (salt) -based copolymer within the above range, the deodorization of the present invention. In the fiber, a component for imparting deodorant performance is less likely to be detached from the fiber, and more excellent deodorant performance can be exhibited.

  The (meth) acrylic acid (salt) copolymer has a weight average molecular weight of preferably 1,000 to 500,000, more preferably 1500 to 300,000, still more preferably 2000 to 100,000, and particularly preferably 2500 to 80,000, most preferably 3000-60000. By adjusting the weight average molecular weight of the (meth) acrylic acid (salt) copolymer within the above range, the deodorant fiber of the present invention is less likely to have components for imparting deodorant performance detached from the fiber. And more excellent deodorization performance can be expressed.

  The (meth) acrylic acid (salt) copolymer may have a structural unit (D) derived from another monomer (d) as long as the effects of the present invention are not impaired. Examples of such other monomer (d) include 3-allyloxy-2-hydroxy-1-propanesulfonic acid (salt), 3-methallyloxy-2-hydroxy-1-propanesulfonic acid (salt), Vinyl sulfonic acid (salt), allyl sulfonic acid (salt), methallyl sulfonic acid (salt), styrene sulfonic acid (salt), 2-acrylamido-2-methylpropane sulfonic acid (salt), sulfoethyl acrylate or a salt thereof, Monoethylenically unsaturated monomer having a sulfonic acid (salt) group such as sulfoethyl methacrylate or a salt thereof, sulfopropyl acrylate or a salt thereof, sulfopropyl methacrylate or a salt thereof, or 2-hydroxy-3-butenesulfonic acid (salt) Body; 2-hydroxyethyl (meth) acrylate, 2-hydroxypropyl (meth) acrylate Hydroxyl group-containing alkyl (meth) acrylates such as Rate, 3-hydroxypropyl (meth) acrylate, 2-hydroxybutyl (meth) acrylate, 4-hydroxybutyl (meth) acrylate, α-hydroxymethylethyl (meth) acrylate; Of an alkyl group having 1 to 18 carbon atoms of (meth) acrylic acid such as methyl (meth) acrylate, ethyl (meth) acrylate, butyl (meth) acrylate, cyclohexyl (meth) acrylate, and lauryl (meth) acrylate. Alkyl (meth) acrylates that are esters; amino group-containing acrylates such as dimethylaminoethyl (meth) acrylate or a quaternized product thereof; amide group-containing monomers such as (meth) acrylamide, dimethylacrylamide, and isopropylacrylamide; Vinyl acetate, etc. Vinyl esters of ethylene; alkenes such as ethylene and propylene; aromatic vinyl monomers such as styrene; maleimide derivatives such as maleimide, phenylmaleimide, and cyclohexylmaleimide; vinyl-based monomers containing nitrile groups such as (meth) acrylonitrile; Monomers; monomers having a sulfonic acid group such as isoprenesulfonic acid and their salts; monomers having a phosphonic acid group such as vinylphosphonic acid and (meth) allylphosphonic acid; (meth) acrolein and the like Aldehyde group-containing vinyl monomers; alkyl vinyl ethers such as methyl vinyl ether, ethyl vinyl ether, butyl vinyl ether; polyalkylene glycol (meth) acrylate, monoalkoxy polyalkylene glycol (meth) acrylate, vinyl alcohol, (meth) a Polyalkylene glycol chain-containing monomers that are monomers having a structure in which 1 to 300 mol of alkylene oxide is added to unsaturated alcohol such as alcohol and isoprenol; vinyl chloride, vinylidene chloride, allyl alcohol, vinyl pyrrolidone, etc. And other monomers having other functional groups. These other arbitrary suitable monomers (d) may be only one kind or two or more kinds.

  The (meth) acrylic acid (salt) copolymer is not easily detached from the fiber. Specifically, the (meth) acrylic acid (salt) copolymer has a fiber separation coefficient of preferably 2.5% or less, more preferably 2.3% or less, and still more preferably 2. It is 1% or less, particularly preferably 2.0% or less, and most preferably 1.8% or less. A method for measuring the fiber separation coefficient will be described later.

The (meth) acrylic acid (salt) -based copolymer can exhibit an excellent cation capturing ability. (Meth) acrylic acid (salt) -based copolymer, cationic supplementary capacity, Ca ion amount in terms of CaCO ₃ are preferably 100mgCaCO ₃ / g~600mgCaCO ₃ / g, more preferably 150mgCaCO ₃ / g a ~500mgCaCO ₃ / g, more preferably from 250mgCaCO ₃ / g~480mgCaCO ₃ / g, particularly preferably 280mgCaCO ₃ / g~470mgCaCO ₃ / g, most preferably 290mgCaCO ₃ / g~460mgCaCO ₃ / g It is. A method for measuring the cation capturing ability will be described later.

  The (meth) acrylic acid (salt) copolymer can be produced by any suitable method. The (meth) acrylic acid (salt) copolymer can be preferably produced by the production method described below.

  The (meth) acrylic acid (salt) copolymer is composed of a monoethylenically unsaturated monocarboxylic acid (salt) monomer (a), a monoethylenically unsaturated dicarboxylic acid (salt) or an anhydride thereof. It can be produced by polymerizing a monomer component containing at least one selected from a monomer (b) and an ether bond-containing hydrophobic monomer (c).

  Monoethylenically unsaturated monocarboxylic acid (salt) monomer (a), monoethylenically unsaturated dicarboxylic acid (salt) or its anhydride monomer (b), ether bond-containing hydrophobic monomer ( For the description of each of c), the above description is incorporated.

  The monomer component is a monoethylenically unsaturated monocarboxylic acid (salt) monomer (a), a monomer (b) that is a monoethylenically unsaturated dicarboxylic acid (salt) or its anhydride, and contains an ether bond In addition to the hydrophobic monomer (c), another monomer (d) may be included.

  The above-mentioned explanation is used for explanation about other monomers (d).

  Monoethylenically unsaturated monocarboxylic acid (salt) monomer (a) and monoethylenically unsaturated dicarboxylic acid (salt) or its anhydride monomer (b) in the monomer component and an ether bond The total content of the contained hydrophobic monomer (c) is preferably 90 mol% to 100 mol%, more preferably 95 mol% to 100 mol%, still more preferably 98 mol% to 100 mol%. %, Particularly preferably substantially 100 mol% (that is, the monomer component comprises a monoethylenically unsaturated monocarboxylic acid (salt) monomer (a) and a monoethylenically unsaturated dicarboxylic acid ( Salt) or its anhydride monomer (b) and ether bond-containing hydrophobic monomer (c)).

  The content ratio of the monoethylenically unsaturated monocarboxylic acid (salt) monomer (a) in the monomer component is preferably 0.1 mol% to 99 mol%, more preferably 1 mol% to 98 mol. Mol%, more preferably 10 mol% to 97 mol%, more preferably 20 mol% to 96 mol%, further preferably 30 mol% to 95 mol%, particularly preferably 40 mol%. It is -93 mol%, Most preferably, it is 50 mol%-90 mol%. By adjusting the content ratio of the monoethylenically unsaturated monocarboxylic acid (salt) monomer (a) in the monomer component within the above range, the deodorizing fiber of the present invention provides deodorizing performance. The component for making it harder to detach | leave from a fiber and can express the more superior deodorizing performance.

  When the monomer component includes a monomer (b) that is a monoethylenically unsaturated dicarboxylic acid (salt) or its anhydride, the monoethylenically unsaturated dicarboxylic acid (salt) or its anhydride in the monomer component The content ratio of the monomer (b) which is a product is preferably 0.1 mol% to 99 mol%, more preferably 1 mol% to 95 mol%, still more preferably 5 mol% to 90 mol%. %, More preferably 10 mol% to 80 mol%, more preferably 15 mol% to 70 mol%, particularly preferably 20 mol% to 60 mol%, and most preferably 30 mol% to 50 mol%. By adjusting the content ratio of the monomer (b) which is a monoethylenically unsaturated dicarboxylic acid (salt) or its anhydride in the monomer component within the above range, the deodorizing fiber of the present invention is A component for imparting deodorizing performance is less likely to be detached from the fiber and can exhibit more excellent deodorizing performance.

  When the monomer component includes an ether bond-containing hydrophobic monomer (c), the content of the ether bond-containing hydrophobic monomer (c) in the monomer component is preferably 0.1 mol% to 50 mol%, more preferably 0.3 mol% to 40 mol%, still more preferably 0.5 mol% to 30 mol%, still more preferably 0.8 mol% to 20 mol% More preferably, it is 1 mol%-10 mol%, Most preferably, it is 2 mol%-8 mol%, Most preferably, it is 3 mol%-7 mol%. By adjusting the content ratio of the ether bond-containing hydrophobic monomer (c) in the monomer component within the above range, the deodorant fiber of the present invention is a component for imparting deodorant performance. It can be more difficult to leave and can exhibit better deodorizing performance.

  Any appropriate polymerization method can be adopted as a polymerization method that can be adopted when the (meth) acrylic acid (salt) copolymer is produced. Examples of such a polymerization method include a method of performing polymerization in an aqueous solvent in the presence of a polymerization initiator and optionally using a chain transfer agent.

  The solvent that can be used in the production of the (meth) acrylic acid (salt) copolymer is preferably an aqueous solvent. Examples of the aqueous solvent include water, alcohol, glycol, glycerin, polyethylene glycol and the like, preferably water. In addition, in order to improve the solubility of the monomer in the solvent, any appropriate organic solvent may be added as appropriate within a range that does not adversely affect the polymerization. Examples of such organic solvents include lower alcohols such as methanol, ethanol and isopropyl alcohol; lower ketones such as acetone, methyl ethyl ketone and diethyl ketone; ethers such as dimethyl ether, diethyl ether and dioxane; amides such as dimethylformaldehyde. And the like. These solvents may use only 1 type and may use 2 or more types.

  The amount of the solvent that can be used in the production of the (meth) acrylic acid (salt) copolymer is preferably 80% by mass to 400% by mass, and more preferably based on the total amount of the monomer components. It is 150 mass%-300 mass%, More preferably, it is 200 mass%-250 mass%. When the amount of the solvent used is less than 80% by mass with respect to the total amount of the monomer components, there is a risk that the viscosity will increase during the polymerization, resulting in insufficient mixing and gel formation. When the amount of the solvent used exceeds 400% by mass with respect to the total amount of the monomer components, there may be a problem that it is difficult to obtain a copolymer having a desired molecular weight.

  Most or all of the solvent may be charged into the reaction vessel at the initial stage of polymerization. For example, a part of the solvent may be appropriately added (dropped) into the reaction system alone during the polymerization. A monomer, a polymerization initiator, a chain transfer agent, and other additives may be appropriately added (dropped) into the reaction system during the polymerization together with these components in a form in which the monomer is dissolved in advance.

  Any appropriate polymerization initiator can be adopted as the polymerization initiator as long as the effects of the present invention are not impaired. Examples of such a polymerization initiator include hydrogen peroxide; persulfates such as sodium persulfate, potassium persulfate, and ammonium persulfate; dimethyl-2,2′-azobis (2-methylpropionate), 2, 2'-azobis (isobutyronitrile), 2,2'-azobis (2-methylbutyronitrile), 2,2'-azobis (2,4-dimethylvaleronitrile), 2,2'-azobis (4 -Methoxy-2,4-dimethylvaleronitrile), 2,2'-azobis (isobutyric acid) dimethyl, 4,4'-azobis (4-cyanovaleric acid), 2,2'-azobis (2-methylpropionamidine) ) Dihydrochloride, 2,2′-azobis [N- (2-carboxyethyl) -2-methylpropionamidine] n hydrate, 2,2′-azobis [2- (2-imidazolin-2-yl) ) Propane] dihydrochloride, 2,2′-azobis [2- (2-imidazolin-2-yl) propane] disulfate dihydrate, 1,1′-azobis (cyclohexane-1-carbonitrile), etc. And azo compounds such as benzoyl peroxide, lauroyl peroxide, peracetic acid, di-t-butyl peroxide, cumene hydroperoxide and the like. Among these polymerization initiators, persulfates such as sodium persulfate, potassium persulfate, and ammonium persulfate are preferable because the effects of the present invention can be sufficiently exhibited.

  Only one polymerization initiator may be used, or two or more polymerization initiators may be used.

  Any appropriate amount of the polymerization initiator can be adopted as long as the copolymerization reaction can be appropriately started. Such an amount is, for example, preferably 15 g or less, more preferably 1 to 12 g in terms of sodium persulfate, with respect to 1 mol of the total amount of monomers.

  When producing a (meth) acrylic acid (salt) -based copolymer, chain transfer is carried out for the purpose of adjusting the molecular weight of the resulting copolymer as long as it does not adversely affect the copolymerization reaction. An agent may be used.

  Any appropriate chain transfer agent can be adopted as the chain transfer agent as long as the effects of the present invention are not impaired. Examples of such chain transfer agents include mercaptoethanol, thioglycerol, thioglycolic acid, 2-mercaptopropionic acid, 3-mercaptopropionic acid, thiomalic acid, octyl thioglycolate, octyl 3-mercaptopropionate, 2- Thiol chain transfer agents such as mercaptoethanesulfonic acid, n-dodecyl mercaptan, octyl mercaptan, butylthioglycolate; halides such as carbon tetrachloride, methylene chloride, bromoform, bromotrichloroethane; secondary alcohols such as isopropanol, glycerin, etc. Phosphorous acid, hypophosphorous acid, and salts thereof (sodium hypophosphite, potassium hypophosphite, etc.), sulfurous acid, bisulfite, dithionite, metabisulfite, and salts thereof (sodium bisulfite) , Potassium bisulfite Ammonium bisulfite, sodium dithionite, potassium dithionite, sodium metabisulfite, metabisulfite potassium, etc.) and the like, lower oxides and salts thereof; and the like. Among these chain transfer agents, bisulfites such as sodium bisulfite, potassium bisulfite, and ammonium bisulfite are preferable because the effects of the present invention can be sufficiently exhibited.

  Only one type of chain transfer agent may be used, or two or more types may be used.

  When a chain transfer agent is used, it is possible to suppress the production of a copolymer having a higher molecular weight than necessary and to produce a low molecular weight copolymer efficiently.

  Any appropriate amount of the chain transfer agent can be adopted as long as it allows the copolymerization reaction of the monomers to proceed appropriately. Such amount is, for example, preferably 0.5 g to 20 g, more preferably 1 g to 15 g, still more preferably 2 g to 10 g, in terms of sodium bisulfite, with respect to 1 mol of the total amount of monomers. It is.

  When producing a (meth) acrylic acid (salt) -based copolymer, as a combination of a polymerization initiator and a chain transfer agent (also referred to as an initiator system), the effect of the present invention can be more fully expressed. It is preferable to use a combination of one or more persulfates and bisulfites.

  Specific examples of the persulfate include sodium persulfate, potassium persulfate, and ammonium persulfate.

  Specific examples of the bisulfite include sodium bisulfite, potassium bisulfite, and ammonium bisulfite.

  When the persulfate and the bisulfite are used in combination, the bisulfite is preferably 0.1 to 5 parts by mass, more preferably 0. 2 parts by mass to 3 parts by mass, and more preferably 0.2 parts by mass to 2 parts by mass. When the amount of bisulfite is less than 0.1 parts by mass with respect to 1 part by mass of persulfate, the effect of bisulfite may be reduced, and therefore the effect of the present invention may not be fully exhibited. There is. Moreover, when bisulfite is less than 0.1 mass part with respect to 1 mass part of persulfate, there exists a possibility that the weight average molecular weight of the (meth) acrylic-acid type copolymer obtained may become high too much. When bisulfite exceeds 5 parts by mass with respect to 1 part by mass of persulfate, the effect of bisulfite may not be obtained enough to meet the usage ratio, and bisulfite is supplied in excess in the polymerization reaction system. Since there is a risk of being consumed (consumed wastefully), excessive bisulfite may be decomposed in the polymerization reaction system, and a large amount of sulfurous acid gas may be generated. Moreover, when bisulfite exceeds 5 mass parts with respect to 1 mass part of persulfate, there exists a possibility that many impurities may produce | generate and there exists a possibility that the performance of the copolymer obtained may fall. Moreover, when bisulfite exceeds 5 mass parts with respect to 1 mass part of persulfate, there exists a possibility that an impurity may precipitate easily when hold | maintaining the obtained copolymer at low temperature.

  The amount of persulfate and bisulfite used in combination is preferably such that the total amount of persulfate and bisulfite is equivalent to sodium persulfate and sodium bisulfite in terms of 1 mol of the total amount of monomers. It is 1g-20g, More preferably, it is 2g-15g, More preferably, it is 3g-11g, Most preferably, it is 4g-8g. When the total amount of persulfate and bisulfite is less than 1 g in terms of sodium persulfate and sodium bisulfite with respect to 1 mol of the total amount of monomers, the effects of the present invention are not sufficiently exhibited. In addition, there is a possibility that the weight average molecular weight of the obtained copolymer becomes too high. When the total amount of persulfate and bisulfite exceeds 20 g with respect to 1 mol of the total amount of monomers, the effects of persulfate and bisulfite may not be obtained enough to match the amount used, Moreover, there exists a possibility that the purity of the copolymer obtained may fall. Further, when the resulting copolymer is kept at a low temperature, there is a possibility that impurities are likely to precipitate.

  The persulfate may be dissolved in a solvent (preferably water) described later and added in the form of a persulfate solution (preferably an aqueous persulfate solution). The concentration of the persulfate when used as such a persulfate solution (preferably an aqueous persulfate solution) is preferably 1% by mass to 35% by mass, more preferably 5% by mass to 30% by mass. Yes, more preferably 10% by mass to 20% by mass. If the concentration of the persulfate solution (preferably persulfate aqueous solution) is less than 1% by mass, transportation and storage may become complicated. When the concentration of the persulfate solution (preferably persulfate aqueous solution) exceeds 35% by mass, handling may be difficult.

  Bisulfite may be dissolved in a solvent (preferably water) described later and added in the form of a bisulfite solution (preferably an aqueous bisulfite solution). The concentration of bisulfite when used as such a bisulfite solution (preferably an aqueous bisulfite solution) is preferably 10% by mass to 42% by mass, more preferably 20% by mass to 41% by mass. More preferably, it is 32 mass%-40 mass%. If the concentration of the bisulfite solution (preferably an aqueous bisulfite solution) is less than 10% by mass, transportation and storage may be complicated. When the concentration of the bisulfite solution (preferably an aqueous bisulfite solution) exceeds 42% by mass, handling may be difficult.

  As a method for adding the polymerization initiator and the chain transfer agent to the reaction vessel, for example, a continuous charging method such as dropping or divided charging can be applied. Further, the chain transfer agent may be introduced alone into the reaction vessel, or may be confused with each monomer, solvent, etc. constituting the monomer component in advance.

  When producing a (meth) acrylic acid (salt) copolymer, any appropriate other additive is used in the polymerization reaction system as long as the effects of the present invention are not impaired. Can do. Examples of such other additives include reaction accelerators, heavy metal concentration adjusting agents, pH adjusting agents, and the like. The reaction accelerator is used for the purpose of, for example, reducing the amount of a polymerization initiator used. The heavy metal concentration adjusting agent is used for the purpose of, for example, reducing the influence on the polymerization reaction that occurs when a small amount of metal is eluted from a reaction vessel or the like. The pH adjuster is used for the purpose of, for example, improving the efficiency of the polymerization reaction and preventing the generation of sulfurous acid gas and corrosion of the apparatus when bisulfite is used as the initiator system.

As the reaction accelerator, for example, a heavy metal compound can be used. Specifically, for example, vanadium oxytrichloride, vanadium trichloride, vanadyl oxalate, vanadyl sulfate, vanadic anhydride, ammonium metavanadate, ammonium sulfate hypovanadas [(NH ₄ ) ₂ SO ₄ · VSO ₄ · 6H ₂ O ], Ammonium sulfate vanadas [(NH ₄ ) V (SO ₄ ) ₂ · 12H ₂ O], copper acetate (II), copper (II), copper bromide (II), copper (II) acetyl acetate, second chloride Copper ammonium, copper ammonium chloride, copper carbonate, copper chloride (II), copper citrate (II), copper formate (II), copper hydroxide (II), copper nitrate, copper naphthenate, copper oleate (II), Copper maleate, copper phosphate, copper sulfate (II), cuprous chloride, copper cyanide (I), copper iodide, copper oxide (I), copper thiocyanate, iron acetyl acetonate, citrate Ammonium iron, Ferric ammonium oxalate, Ammonium iron sulfate, Molle salt, Ammonium ferric sulfate, Iron citrate, Iron fumarate, Iron maleate, Ferrous lactate, Ferric nitrate, Iron pentacarbonyl, Phosphorus Water-soluble polyvalent metal salts such as ferric acid and ferric pyrophosphate; polyvalent metal oxides such as vanadium pentoxide, copper (II) oxide, ferrous oxide and ferric oxide; iron sulfide (III ), Iron (II) sulfide, copper sulfide and other polyvalent metal sulfides; copper powder; iron powder; and the like. Only one type of reaction accelerator may be used, or two or more types may be used.

As the heavy metal concentration adjusting agent, for example, a polyvalent metal compound or a simple substance can be used. Specifically, for example, vanadium oxytrichloride, vanadium trichloride, vanadyl oxalate, vanadyl sulfate, vanadic anhydride, ammonium metavanadate, ammonium sulfate hypovanadas [(NH ₄ ) ₂ SO ₄ · VSO ₄ · 6H ₂ O ], Ammonium sulfate vanadas [(NH ₄ ) V (SO ₄ ) ₂ · 12H ₂ O], copper acetate (II), copper (II), copper bromide (II), copper (II) acetyl acetate, second chloride Copper ammonium, copper ammonium chloride, copper carbonate, copper chloride (II), copper citrate (II), copper formate (II), copper hydroxide (II), copper nitrate, copper naphthenate, copper oleate (II), Copper maleate, copper phosphate, copper sulfate (II), cuprous chloride, copper cyanide (I), copper iodide, copper oxide (I), copper thiocyanate, iron acetyl acetonate, citrate Ammonium iron, Ferric ammonium oxalate, Ammonium iron sulfate, Molle salt, Ammonium ferric sulfate, Iron citrate, Iron fumarate, Iron maleate, Ferrous lactate, Ferric nitrate, Iron pentacarbonyl, Phosphorus Water-soluble polyvalent metal salts such as ferric acid and ferric pyrophosphate; polyvalent metal oxides such as vanadium pentoxide, copper (II) oxide, ferrous oxide and ferric oxide; iron sulfide (III ), Iron (II) sulfide, copper sulfide and other polyvalent metal sulfides; copper powder; iron powder; and the like. Only one type of heavy metal concentration adjusting agent may be used, or two or more types may be used.

  Examples of pH adjusters include alkali metal hydroxides such as sodium hydroxide and potassium hydroxide; alkaline earth metal hydroxides such as calcium hydroxide and magnesium hydroxide; ammonia, monoethanolamine, and triethanol. Organic amine salts such as amines; and the like. Among these, alkali metal hydroxides such as sodium hydroxide and potassium hydroxide are preferable, and sodium hydroxide is particularly preferable. The pH adjusting agent may be referred to as a “neutralizing agent”. Only 1 type may be used for a pH adjuster, and 2 or more types may be used for it.

  When producing a (meth) acrylic acid (salt) -based copolymer, the polymerization temperature of the polymerization reaction can be set to any appropriate temperature as long as the effects of the present invention are not impaired. The lower limit of the polymerization temperature is preferably 50 ° C. or higher, more preferably 70 ° C. or higher, and the upper limit of the polymerization temperature is preferably 99 ° C. or lower in terms of efficiently producing a copolymer. Preferably it is 95 degrees C or less. Moreover, you may set the upper limit of superposition | polymerization temperature to arbitrary appropriate temperatures below the boiling point of a polymerization reaction solution.

  In the production of a (meth) acrylic acid (salt) copolymer, in the case of a method of starting polymerization from room temperature (room temperature starting method), for example, when polymerization is performed in 240 minutes per batch (180 minute prescription) ), Preferably between 0 minutes and 70 minutes, more preferably between 0 minutes and 50 minutes, and even more preferably between 0 minutes and 30 minutes, within the set temperature (polymerization temperature range). , Preferably 70 ° C. to 95 ° C., more preferably 80 ° C. to 90 ° C.). Thereafter, this set temperature is preferably maintained until the polymerization is completed.

  In producing a (meth) acrylic acid (salt) copolymer, the pressure in the reaction system can be set to any appropriate pressure within a range not impairing the effects of the present invention. Examples of such pressure include normal pressure (atmospheric pressure), reduced pressure, and increased pressure.

  When producing a (meth) acrylic acid (salt) -based copolymer, the atmosphere in the reaction system can be set to any appropriate atmosphere as long as the effects of the present invention are not impaired. Examples of such an atmosphere include an air atmosphere and an inert gas atmosphere.

  In producing a (meth) acrylic acid (salt) copolymer, the monomer polymerization reaction is preferably performed under acidic conditions. By performing the polymerization reaction under acidic conditions, an increase in the viscosity of the solution in the polymerization reaction system can be suppressed, and a low molecular weight copolymer can be produced satisfactorily. In addition, since the polymerization reaction can proceed under a higher concentration condition than before, the production efficiency can be significantly increased. For example, by adjusting the degree of neutralization during polymerization within the range of 0 mol% to 25 mol%, the effect of reducing the amount of polymerization initiator can be increased synergistically, and the effect of reducing impurities can be significantly improved. it can. Furthermore, it is preferable to adjust the pH at 25 ° C. of the reaction solution during polymerization within the range of 1 to 6. By carrying out the polymerization reaction under such acidic conditions, the polymerization can be carried out at a high concentration and in one stage. For this reason, it is also possible to omit the concentration step which was necessary in some cases in the conventional manufacturing method. Therefore, the productivity of the copolymer can be greatly improved, and an increase in production cost can be suppressed.

  The pH of the reaction solution during polymerization at 25 ° C. is preferably in the range of 1 to 6, more preferably in the range of 1 to 5, and still more preferably in the range of 1 to 4. When the pH of the reaction solution during polymerization at 25 ° C. is less than 1, for example, when bisulfite is used as an initiator system, sulfurous acid gas may be generated or the apparatus may be corroded. When the pH at 25 ° C. of the reaction solution during polymerization exceeds 6, when bisulfite is used as an initiator system, the use efficiency of bisulfite may be lowered, and the molecular weight may be increased. There is.

  The pH of the reaction solution during polymerization at 25 ° C. may be adjusted using, for example, the aforementioned pH adjuster.

  The degree of neutralization during the polymerization is preferably in the range of 0 mol% to 25 mol%, more preferably in the range of 1 mol% to 20 mol%, and still more preferably in the range of 2 mol% to 15 mol%. If the degree of neutralization during polymerization is within such a range, the monomer can be copolymerized well, and impurities can be reduced. Further, the viscosity of the solution in the polymerization reaction system does not increase, and a low molecular weight copolymer can be produced satisfactorily. In addition, since the polymerization reaction can proceed under a higher concentration condition than before, the production efficiency can be significantly increased.

  Any appropriate method can be adopted as the neutralization method as long as the effects of the present invention are not impaired. For example, a salt of (meth) acrylic acid such as sodium (meth) acrylate may be used as a part of the raw material, and an alkali metal hydroxide such as sodium hydroxide is used as a neutralizing agent. You may neutralize during superposition | polymerization and you may use these together. In addition, the neutralizing agent may be added in a solid form or may be added in an aqueous solution dissolved in an appropriate solvent (preferably water).

  The concentration of the aqueous solution when the polymerization reaction is performed in the form of an aqueous solution is preferably 10% by mass to 60% by mass, more preferably 20% by mass to 55% by mass, and further preferably 30% by mass to 50% by mass. It is. When the concentration of the aqueous solution is less than 10% by mass, transportation and storage may be complicated. When the concentration of the aqueous solution exceeds 60% by mass, handling may be difficult.

  In the polymerization, a monomer, a polymerization initiator, a chain transfer agent, and, if necessary, other additives are previously added to an appropriate solvent (preferably the same type of solvent as the liquid to be dropped). Dissolve the monomer solution, the polymerization initiator solution, the chain transfer agent solution, and, if necessary, other additive solutions. It is preferable to perform polymerization while continuously dropping over a predetermined dropping time. Further, a part of the solvent may be dropped later, separately from the initially charged solvent prepared in advance in a container in the reaction system. Regarding the dropping method, it may be dropped continuously, or may be dropped intermittently in several portions. In addition, one or two or more of the monomers may be initially charged. Further, the dropping rate of one or more monomers may be always constant from the start to the end of dropping, or the dropping rate may be changed over time according to the polymerization temperature or the like. Moreover, it is not necessary to drop all the dropping components in the same manner, and the starting time and the ending time may be shifted for each dropping component, or the dropping time may be shortened or extended. In addition, when each component is added dropwise in the form of a solution, the added solution may be heated to the same level as the polymerization temperature in the reaction system. In this way, when the polymerization temperature is kept constant, temperature fluctuation is reduced and temperature adjustment is easy.

  When bisulfite is used as the initiator system, the weight average molecular weight of the copolymer at the initial stage of polymerization affects the final weight average molecular weight of bisulfite. For this reason, in order to reduce the weight average molecular weight of the copolymer at the initial stage of polymerization, bisulfite or a solution thereof is preferably within 60 minutes, more preferably within 30 minutes, and even more preferably from the start of polymerization. It is preferable to add (drop) 5 mass% to 35 mass% within 10 minutes.

  When bisulfite is used as the initiator system, the bisulfite or its solution dropping end time is preferably from 1 minute to 30 minutes, more preferably from 1 minute to 20 minutes, than the monomer dropping end time. Further, it is preferable to speed up by 1 to 15 minutes. As a result, the amount of bisulfite remaining after the completion of the polymerization can be reduced, and generation of sulfurous acid gas and formation of impurities due to such residual bisulfite can be effectively and effectively suppressed.

  When using a persulfate as an initiator system, the dropping end time of the persulfate or a solution thereof is preferably 1 minute to 60 minutes, more preferably 1 minute to 45 minutes, than the dropping end time of the monomer. More preferably, it may be delayed for 1 to 20 minutes. Thereby, the quantity of the monomer which remains after completion | finish of superposition | polymerization can be reduced, and the impurity resulting from such a residual monomer can be reduced.

  The total dropping time during the polymerization is preferably 150 minutes to 600 minutes, more preferably 180 minutes to 450 minutes, and further preferably 210 minutes to 300 minutes. When the total dropping time is less than 150 minutes, the weight average molecular weight of the obtained copolymer may be too high. Further, excessive bisulfite may be decomposed to generate sulfurous acid gas. When the total dropping time exceeds 600 minutes, the productivity of the resulting (meth) acrylic acid copolymer may be lowered. The total dropping time here refers to the time from the start of dropping the first dropping component (not necessarily one component) to the completion of dropping the last dropping component (not necessarily one component).

  The solid content concentration in the polymerization solution when the polymerization reaction is completed is preferably 35% by mass or more, more preferably 40% by mass to 70% by mass, and further preferably 45% by mass to 65% by mass. It is. If the solid content concentration in the polymerization solution at the end of the polymerization reaction is 35% by mass or more, the polymerization can be performed at a high concentration and in one step. Therefore, a low molecular weight (meth) acrylic acid copolymer can be obtained efficiently. For example, it is possible to omit the concentration step that is necessary in some cases in the conventional manufacturing method, and to increase the manufacturing efficiency. As a result, the productivity of the copolymer is improved, and it is possible to suppress an increase in manufacturing cost. Here, the time point at which the polymerization reaction is completed may be a time point at which the dropping of all the dropping components is completed, but preferably, a time point at which a predetermined aging time has elapsed (a time point at which the polymerization is completed). means.

  In producing a (meth) acrylic acid (salt) copolymer, an aging step for aging the polymerization reaction solution may be provided after the polymerization reaction is completed in order to effectively complete the polymerization. The aging time in the aging step is preferably 1 minute to 120 minutes, more preferably 5 minutes to 90 minutes, and further preferably 10 minutes to 60 minutes, in order to effectively complete the polymerization. In addition, as for the temperature in an ripening process, Preferably said polymerization temperature is applied. In the production of a (meth) acrylic acid (salt) -based copolymer, when an aging step is present, the polymerization time means the above total dropping time + aging time.

  EXAMPLES Hereinafter, although an Example is given and this invention is demonstrated concretely, this invention is not limited to these Examples. Unless otherwise specified, “part” means “part by mass” and “%” means “% by mass”.

<Measurement conditions of weight average molecular weight (GPC)>
The weight average molecular weight was measured using gel permeation chromatography (GPC) under the following conditions.
Apparatus: L-7000 series manufactured by Hitachi, Ltd. Detector: HITACHI RI Detector L-7490
Column: SHODEX Asahipak GF-310-HQ, GF-710-HQ, GF-1G 7B manufactured by Showa Denko Co., Ltd.
Column temperature: 40 ° C
Flow rate: 0.5 ml / min
Calibration curve: Polyacrylic acid standard made by Sowa Chemical Co., Ltd.
Eluent: 0.1N sodium acetate / acetonitrile = 3/1 (mass ratio).

<Quantification of monomer>
The monomer was quantified using liquid chromatography under the following conditions.
Measuring device: L-7000 series detector manufactured by Hitachi, Ltd .: UV detector L-7400 manufactured by Hitachi, Ltd.
Column: SHODEX RSpak DE-413 manufactured by Showa Denko Co., Ltd.
Temperature: 40.0 ° C
Eluent: 0.1% phosphoric acid aqueous solution Flow rate: 1.0 ml / min

<Measurement of 3-sulfonepropionic acid (3SPA) concentration>
The concentration of 3-sulfonepropionic acid (3SPA) was measured under the following conditions.
Apparatus: Waters gradient HPLC system Column: TSK-GEL ODS-100V 5 μm 4.6 × 250 mm 2 in series Eluent: 0.02 M potassium dihydrogen phosphate (adjusted to pH 2.5)
Flow rate: 0.7 mL / min
Temperature: 30 ° C
Detector: UV detector (210 nm)

<Method for measuring solid content>
The copolymer (1.0 g of copolymer added with 1.0 g of water) was allowed to stand for 2 hours in an oven heated to 120 ° C. and dried. From the mass change before and after drying, the solid content (%) and the volatile component (%) were calculated.

<Fiber separation factor (%)>
The fiber release coefficient was measured as an index indicating the difficulty of releasing the copolymer from the fiber.
5 g of an aqueous copolymer solution adjusted to a solid content of 1% was applied to a 2 cm × 2 cm JIS cotton cloth and dried in a dryer at 100 ° C. for 1 hour. The treated cloth was immersed in 10 g of ion exchange water (25 ° C.) and allowed to stand at 25 ° C. for 30 minutes. After 30 minutes, the cloth was immediately taken out, the amount of the copolymer eluted in the aqueous solution was measured by solid content measurement after drying with hot air at 130 ° C. for 1 hour, and the mass ratio of the detached copolymer was determined. Calculated.

<Measurement of cation scavenging ability>
In a beaker having a capacity of 100 cc, 50 g of a 0.001 mol / L calcium chloride aqueous solution was collected, and 10 mg of an aqueous copolymer solution was added in terms of solid content. Next, the pH of this aqueous solution was adjusted to 9-11 with dilute sodium hydroxide. Then, 1 ml of 4 mol / L potassium chloride aqueous solution was added as a calcium ion electrode stabilizer under stirring. Using a titration device (Hiranuma AUTO TITRATOR COM-1700) and a calcium ion composite electrode (ORIION 9720BNWP), free calcium ions are measured, and how many mg of calcium ions are captured per 1 g of copolymer in terms of calcium carbonate. Was calculated by calculation. The unit of cation scavenging ability is “mgCaCO ₃ / g”.

[Synthesis Example 1]
(1) Synthesis of monomer In a 500 mL glass four-necked flask equipped with a reflux condenser and a stirrer (paddle blade), n-butyl alcohol: 370.0 g and pelleted sodium hydroxide: 4. 27 g was charged and heated to 60 ° C. with stirring. Next, allyl glycidyl ether (hereinafter also referred to as “AGE”): 57.0 g was added over 30 minutes, and then reacted for 5 hours. This solution was transferred to a 1000 ml eggplant flask and desolvated with a rotary evaporator. 20 mass% sodium chloride aqueous solution: 200.0g was added here, this aqueous solution was moved to a 500 ml separating funnel, and after shaking well, it left still until it separated and the lower layer was removed. The remaining upper layer was transferred to a 300 ml eggplant flask and desolvated with a rotary evaporator. The precipitated salt was removed by filtration to obtain monomer (1).
(2) Polymerization A 1000-mL glass separable flask equipped with a reflux condenser and a stirrer (paddle blade) was charged with 127.0 g of pure water, 0.0043 g of a Mole salt, and 127.5 g of maleic anhydride, With stirring, 48% sodium hydroxide aqueous solution (hereinafter also referred to as “48% NaOH”): 160.1 g was added from the dropping funnel over 30 minutes. While stirring, the temperature was raised to 103 ° C., boiling reflux was confirmed, and a polymerization reaction system was obtained. Next, in a polymerization reaction system maintained at a boiling point (105 ° C.) with stirring, an 80% aqueous acrylic acid solution (hereinafter also referred to as “80% AA”): 117.1 g, monomer (1): 25.8 g, 15% sodium persulfate aqueous solution (hereinafter also referred to as “15% NaPS”): 43.8 g, and 35% hydrogen peroxide (hereinafter also referred to as “35% H ₂ O ₂ ”) : 15.6 g of each was started to be dropped simultaneously from separate nozzles, and polymerization was started. The dropping time of each solution was 120 minutes for 80% AA, 90 minutes for monomer (1), 120 minutes for 15% NaPS, and 120 minutes for 35% H ₂ O ₂ . Moreover, the dropping rate of each solution was made constant, and each solution was dropped continuously.
After completion of the 80% AA dropwise addition, the reaction solution was kept at the boiling point (102 ° C.) for 30 minutes (ripening) to complete the polymerization. After completion of the polymerization, the polymerization reaction solution was stirred and allowed to cool.
In this way, an aqueous copolymer solution (1) containing a copolymer (1) and having a solid content concentration of 56% was obtained. The weight average molecular weight of the copolymer (1) was 4000.

[Synthesis Example 2]
A glass separable flask having a capacity of 1000 mL equipped with a reflux condenser and a stirrer (paddle blade) was charged with 128.4 g of pure water and 0.0187 g of Mole salt, and the temperature was raised to 85 ° C. while stirring, did. Next, 80% AA: 270.0 g, monomer (1): 62.7 g, 15% NaPS: 80 g, and 35% sodium bisulfite in a polymerization reaction system maintained at 85 ° C. with stirring. Aqueous solution (hereinafter also referred to as “35% SBS”): 30 g was dropped from each separate nozzle. The dropping time of each solution was 180 minutes for 80% AA, 120 minutes for monomer (1), 190 minutes for 15% NaPS, and 175 minutes for 35% SBS. Moreover, the dropping rate of each solution was made constant, and each solution was dropped continuously.
After the completion of the addition of 80% AA, the reaction solution was kept at 85 ° C. (ripening) for another 30 minutes to complete the polymerization. After completion of the polymerization, 48% NaOH: 193.3 g was gradually added dropwise while stirring and allowing the polymerization reaction liquid to cool, thereby neutralizing the polymerization reaction liquid.
In this way, an aqueous copolymer solution (2) containing a copolymer (2) and having a solid content concentration of 45% was obtained. The weight average molecular weight of the copolymer (2) was 10,000. The residual acrylic acid was 120 ppm, and the residual 3 SPA was 0.16%.

[Synthesis Example 3]
A glass separable flask with a capacity of 2000 mL equipped with a reflux condenser and a stirrer (paddle blade) was charged with 296.0 g of pure water and 126 g of maleic anhydride, and dropped into a dropping funnel with 214.3 g of 48% NaOH. It was added over 30 minutes. While stirring, the temperature was raised to 103 ° C., boiling reflux was confirmed, and a polymerization reaction system was obtained. Next, 80% AA: 270 g, 15% NaPS: 43.8 g, and 35% H ₂ O ₂ : 15.6 g were respectively added to the polymerization reaction system maintained at the boiling point (103 ° C.) under stirring. Dropping was started simultaneously from separate nozzles, and polymerization was started. The dropping time of each solution was 120 minutes for 80% AA, 130 minutes for 15% NaPS, and 120 minutes for 35% H ₂ O ₂ . Moreover, the dropping rate of each solution was made constant, and each solution was dropped continuously.
After the completion of the dropwise addition of 80% AA, the reaction solution was kept at the boiling point (102 ° C.) for 30 minutes (ripening) to complete the polymerization. After completion of the polymerization, the polymerization reaction solution was stirred and allowed to cool.
In this way, a copolymer aqueous solution (3) having a solid content concentration of 45% containing the copolymer (3) was obtained. The weight average molecular weight of the copolymer (3) was 60000.

[Synthesis Example 4]
A glass separable flask with a capacity of 2000 mL equipped with a reflux condenser and a stirrer (paddle blade) was charged with 296.0 g of pure water and 196 g of maleic anhydride, and a dropping funnel was added with 333.3 g of 48% NaOH while stirring. It was added over 30 minutes. While stirring, the temperature was raised to 104 ° C., boiling reflux was confirmed, and a polymerization reaction system was obtained. Next, 80% AA: 270 g, 15% NaPS: 43.8 g, and 35% H ₂ O ₂ : 15.6 g were respectively added to the polymerization reaction system maintained at the boiling point (104 ° C.) under stirring. Dropping was started simultaneously from separate nozzles, and polymerization was started. The dropping time of each solution was 120 minutes for 80% AA, 130 minutes for 15% NaPS, and 120 minutes for 35% H ₂ O ₂ . Moreover, the dropping rate of each solution was made constant, and each solution was dropped continuously.
After completion of the 80% AA dropwise addition, the reaction solution was kept at the boiling point (102 ° C.) for 30 minutes (ripening) to complete the polymerization. After completion of the polymerization, the polymerization reaction solution was stirred and allowed to cool.
In this way, a copolymer aqueous solution (4) having a solid content concentration of 48% containing the copolymer (4) was obtained. The weight average molecular weight of the copolymer (4) was 50,000.

[Synthesis Example 5]
A 2000 mL glass separable flask equipped with a reflux condenser and a stirrer (paddle blade) was charged with pure water: 296.0 g and maleic anhydride: 294 g, and 48% NaOH: 500 g was added from a dropping funnel while stirring. It was charged over 30 minutes. While stirring, the temperature was raised to 104 ° C., boiling reflux was confirmed, and a polymerization reaction system was obtained. Next, 80% AA: 270 g, 15% NaPS: 43.8 g, and 35% H ₂ O ₂ : 150 g were separately added to the polymerization reaction system maintained at the boiling point (104 ° C.) under stirring. Dropping was started simultaneously from the nozzle, and polymerization was started. The dropping time of each solution was 120 minutes for 80% AA, 130 minutes for 15% NaPS, and 100 minutes for 35% H ₂ O ₂ . Moreover, the dropping rate of each solution was made constant, and each solution was dropped continuously.
After the completion of the dropwise addition of 80% AA, the reaction solution was kept at the boiling point (102 ° C.) for 30 minutes (ripening) to complete the polymerization. After completion of the polymerization, the polymerization reaction solution was stirred and allowed to cool.
Thus, a copolymer aqueous solution (5) containing a copolymer (5) and having a solid content concentration of 46% was obtained. The weight average molecular weight of the copolymer (5) was 5000.

[Comparative Synthesis Example 1]: Sodium polyacrylate A 1000 mL glass separable flask equipped with a reflux condenser and a stirrer (paddle blade) was charged with 146.8 g of pure water and Mole salt: 0.0186 g and stirred. While raising the temperature to 85 ° C., a polymerization reaction system was obtained. Next, 80% AA: 270.0 g, 48% NaOH: 12.5 g, 15% NaPS: 40 g, and 35% SBS: 30 g were respectively added to the polymerization reaction system maintained at 85 ° C. with stirring. Dropped from separate nozzles. The dropping time of each solution was 180 minutes for 80% AA and 48% NaOH, 190 minutes for 15% NaPS, and 175 minutes for 35% SBS. Moreover, the dropping rate of each solution was made constant, and each solution was dropped continuously.
After the completion of the addition of 80% AA, the reaction solution was kept at 85 ° C. (ripening) for another 30 minutes to complete the polymerization. After completion of the polymerization, 48% NaOH: 197.5 g was gradually added dropwise while stirring and allowing the polymerization reaction liquid to cool, thereby neutralizing the polymerization reaction liquid.
In this way, an aqueous polymer solution (C1) containing a polymer (C1) and having a solid content concentration of 45% was obtained. The weight average molecular weight of the polymer (C1) was 5000.

[Comparative Synthesis Example 2]: Sodium polyacrylate A 1000 mL glass separable flask equipped with a reflux condenser and a stirrer (paddle blade) was charged with 146.8 g of pure water and 0.0186 g of Mole salt and stirred. While raising the temperature to 85 ° C., a polymerization reaction system was obtained. Next, 80% AA: 270.0 g, 48% NaOH: 12.5 g, 15% NaPS: 40 g, and 35% SBS: 70 g were respectively added to the polymerization reaction system maintained at 85 ° C. with stirring. Dropped from separate nozzles. The dropping time of each solution was 180 minutes for 80% AA and 48% NaOH, 190 minutes for 15% NaPS, and 175 minutes for 35% SBS. Moreover, the dropping rate of each solution was made constant, and each solution was dropped continuously.
After the completion of the addition of 80% AA, the reaction solution was kept at 85 ° C. (ripening) for another 30 minutes to complete the polymerization. After completion of the polymerization, 48% NaOH: 197.5 g was gradually added dropwise while stirring and allowing the polymerization reaction liquid to cool, thereby neutralizing the polymerization reaction liquid.
Thus, a polymer aqueous solution (C2) having a solid content concentration of 45% containing the polymer (C2) was obtained. The weight average molecular weight of the polymer (C2) was 2000.

[Comparative Synthesis Example 3]: Sodium polyacrylate A 1000 mL glass separable flask equipped with a reflux condenser and a stirrer (paddle blade) was charged with 146.8 g of pure water and 0.0186 g of Mole salt and stirred. While raising the temperature to 85 ° C., a polymerization reaction system was obtained. Next, 80% AA: 270.0 g, 48% NaOH: 12.5 g, 15% NaPS: 20 g, and 35% SBS: 10 g were respectively added to the polymerization reaction system maintained at 85 ° C. with stirring. Dropped from separate nozzles. The dropping time of each solution was 180 minutes for 80% AA and 48% NaOH, 190 minutes for 15% NaPS, and 175 minutes for 35% SBS. Moreover, the dropping rate of each solution was made constant, and each solution was dropped continuously.
After the completion of the addition of 80% AA, the reaction solution was kept at 85 ° C. (ripening) for another 30 minutes to complete the polymerization. After completion of the polymerization, 48% NaOH: 197.5 g was gradually added dropwise while stirring and allowing the polymerization reaction liquid to cool, thereby neutralizing the polymerization reaction liquid.
Thus, a polymer aqueous solution (C3) having a solid content concentration of 45% containing the polymer (C3) was obtained. The weight average molecular weight of the polymer (C3) was 50,000.

[Example 1]
The copolymer (1) obtained in Synthesis Example 1 is added to the raw material viscose so that the main component is 6% by mass with respect to the cellulose, and the mixture is stirred and mixed in a mixer to obtain a viscose for spinning. A liquid was prepared. The temperature was kept at 20 ° C. As the raw material viscose, a viscose stock solution containing 8.5% by mass of cellulose, 5.7% by mass of sodium hydroxide, and 2.8% by mass of carbon disulfide was used.
The obtained viscose solution for spinning was spun at a spinning speed of 60 m / min and a draw rate of 50% by a two-bath tension spinning method to obtain a viscose rayon yarn having a fineness of 1.4 dtex. As the first bath (spinning bath), a Mueller bath (50 ° C.) containing 100 g / L of sulfuric acid, 15 g / L of zinc sulfate, and 350 g / L of sodium sulfate was used. A circular nozzle (hole diameter: 0.06 mm, number of holes: 4000) was used as a spinneret for discharging viscose. During spinning, there was no inconvenience such as single yarn breakage, and the spinnability of the mixed viscose was good.
The viscose rayon yarn obtained above was cut into a fiber length of 38 mm and scoured. In the scouring process, water washing was performed after the hot water treatment, and desulfurization was performed by showering sodium hydrosulfide. The obtained treated cotton is washed again with water, oil is applied in a shower, excess moisture and oil are removed from the fiber with a compression roller, and drying treatment (60 ° C., 7 hours) is performed to obtain fiber (1). It was.
The results are shown in Table 1.

[Example 2]
A fiber (2) was obtained in the same manner as in Example 1 except that the copolymer (2) obtained in Synthesis Example 2 was used instead of the copolymer (1) obtained in Synthesis Example 1. It was.
The results are shown in Table 1.

Example 3
A fiber (3) was obtained in the same manner as in Example 1 except that the copolymer (3) obtained in Synthesis Example 3 was used instead of the copolymer (1) obtained in Synthesis Example 1. It was.
The results are shown in Table 1.

Example 4
A fiber (4) was obtained in the same manner as in Example 1 except that the copolymer (4) obtained in Synthesis Example 4 was used instead of the copolymer (1) obtained in Synthesis Example 1. It was.
The results are shown in Table 1.

Example 5
A fiber (5) was obtained in the same manner as in Example 1 except that the copolymer (5) obtained in Synthesis Example 5 was used in place of the copolymer (1) obtained in Synthesis Example 1. It was.
The results are shown in Table 1.

[Comparative Example 1]
A fiber (C1) was obtained in the same manner as in Example 1 except that the polymer (C1) obtained in Comparative Synthesis Example 1 was used in place of the copolymer (1) obtained in Synthesis Example 1. It was.
The results are shown in Table 2.

[Comparative Example 2]
A fiber (C2) was obtained in the same manner as in Example 1 except that the polymer (C2) obtained in Comparative Synthesis Example 2 was used instead of the copolymer (1) obtained in Synthesis Example 1. It was.
The results are shown in Table 2.

[Comparative Example 3]
A fiber (C3) was obtained in the same manner as in Example 1 except that the polymer (C3) obtained in Comparative Synthesis Example 3 was used instead of the copolymer (1) obtained in Synthesis Example 1. It was.
The results are shown in Table 2.

  As shown in Tables 1 and 2, the copolymers contained in the fibers obtained in the examples have a cation scavenging ability that represents deodorizing performance as compared with the polymers contained in the fibers obtained in the comparative examples. It turns out that it is a sufficient level. Moreover, it turns out that the copolymer contained in the fiber obtained in the Example shows a very excellent fiber separation coefficient as compared with the polymer contained in the fiber obtained in the comparative example.

The deodorizing fiber of the present invention is useful for fiber products having a deodorizing function.

Claims (4)

(Meth) acrylic acid (salt) -based copolymer used for fibers containing cellulose,
The (meth) acrylic acid (salt) copolymer comprises a structural unit (A) derived from a monoethylenically unsaturated monocarboxylic acid (salt) monomer (a) and a monoethylenically unsaturated dicarboxylic acid (salt). Or at least one selected from the structural unit (B) derived from the monomer (b) which is an anhydride thereof and the structural unit (C) derived from the ether bond-containing hydrophobic monomer (c). polymer der is,
The ether bond-containing hydrophobic monomer (c) is 1-allyloxy-3-butoxypropan-2-ol represented by the chemical formula (2), a hexene oxide adduct of isoprenol represented by the chemical formula (3), Is at least one selected from allyl butyl ether represented by the chemical formula (4) ,
(Meth) acrylic acid (salt) copolymer .

The total of the structural unit (A), the structural unit (B), and the structural unit (C) with respect to the total of structural units derived from all monomers in the (meth) acrylic acid (salt) -based copolymer. The (meth) acrylic acid (salt) copolymer according to claim 1, wherein the content ratio is 90 mol% to 100 mol%. The (meth) weight average molecular weight of the acrylic acid (salt) -based copolymer is 1,000 to 500,000, according to claim 1 or according to 2 (meth) acrylic acid (salt) copolymer. The (meth) acrylic acid (salt) system according to any one of claims 1 to 3, wherein the ether bond-containing hydrophobic monomer (c) is 1-allyloxy-3-butoxypropan-2-ol. Copolymer .