WO2013145675A1

WO2013145675A1 - Copolymer for gypsum dispersant and method for producing same, gypsum dispersant, and gypsum composition

Info

Publication number: WO2013145675A1
Application number: PCT/JP2013/001967
Authority: WO
Inventors: 和伸河原; 林谷　俊男
Original assignee: 株式会社日本触媒
Priority date: 2012-03-28
Filing date: 2013-03-22
Publication date: 2013-10-03
Also published as: JP5947374B2; JPWO2013145675A1

Abstract

Provided are: a copolymer for a gypsum dispersant with which it is possible to achieve both improvement of fluidity of a gypsum slurry and shortening of the setting time; and a method for producing the same. This copolymer for a gypsum dispersant comprises a structural unit derived from a monomer (a) represented by general formula (A) and a structural unit derived from a monomer (b) represented by general formula (B), and contains a copolymer with a weight average molecular weight of 1 to 200,000, the amount of elemental sulfur in the copolymer being 0.2 weight% or less with respect to the copolymer.

Description

Copolymer for gypsum dispersant and method for producing the same, gypsum dispersant, gypsum composition

The present invention relates to a copolymer used as a gypsum dispersant, a method for producing the same, a gypsum dispersant, and a gypsum composition.

Gypsum molded products such as gypsum board, gypsum plaster and gypsum block are manufactured by a method in which gypsum slurry is poured into a mold, and dried and coagulated. At this time, in order to facilitate the pouring of the gypsum slurry into the mold, it is necessary to impart sufficient fluidity to the gypsum slurry. As a method of increasing the fluidity of the gypsum slurry, it is conceivable to increase the amount of water, but if the ratio of water is increased, the strength of the gypsum molded product will decrease, so instead of increasing the water, A technique of adding a gypsum dispersant is widely used. As a gypsum dispersant, for example, a copolymer of polyalkylene glycol mono (meth) acrylic acid ester and (meth) acrylic acid is known (for example, see Patent Document 1).

JP-A-8-217505

The gypsum dispersant is required to improve the fluidity of the gypsum slurry and to shorten the setting time of the gypsum slurry. However, although the conventional copolymer for gypsum dispersant can improve the fluidity, it still has a problem that the setting time is long.

Therefore, an object of the present invention is to provide a copolymer for a gypsum dispersant that can achieve both improvement in fluidity of gypsum slurry and shortening of the setting time, and a method for producing the same.

The copolymer for a gypsum dispersant according to the present invention comprises a structural unit derived from the monomer (a) represented by the following general formula (A) and a monomer (b) represented by the following general formula (B). ) And a copolymer having a weight average molecular weight of 1 to 200,000, and the amount of sulfur element in the copolymer is 0.2% by weight or less based on the copolymer. .

In addition, a method for producing a copolymer for a gypsum dispersant having a weight average molecular weight of 1 to 200,000 according to the present invention includes a monomer (a) represented by the following general formula (A), a general formula ( The monomer component containing the monomer (b) represented by B) is polymerized by mixing the polymerization initiator, and the addition amount of the thiol compound added to the monomer component is It is 1.2 mol% or less with respect to a monomer component.

In the formula, R ₁ and R ₂ are the same or different and represent hydrogen or a methyl group, and AO is the same or different and is one or more types of oxyalkylene groups having 2 or more carbon atoms or two or more types having 2 or more carbon atoms. X represents an integer of 0 to 2, y represents 0 or 1, n is a number of 15 to 200 representing the average number of moles added of the oxyalkylene group, R ₃
Represents a hydrogen atom or a hydrocarbon group having 1 to 20 carbon atoms.

In the formula, R ₄ , R ₅ and R ₆ are the same or different and each represents a hydrogen atom, a methyl group or — (CH ₂ ) _n COOM ₂ , and — (CH ₂ ) _m COOM ₂ represents —COOM ₁ or other -(CH ₂ ) _n COOM ₂ may form an anhydride, and in this case, M ₁ and M ₂ of these groups are not present. m represents an integer of 0 to 2, and M ₁ and M ₂ are the same or different and each represents a hydrogen atom, an alkali metal, an alkaline earth metal, an ammonium group, or an organic ammonium group.

According to the present invention, it is possible to realize a copolymer for a gypsum dispersant that can improve both the fluidity of the gypsum slurry and shorten the setting time, and a method for producing the same.

Hereinafter, embodiments of the present invention will be described. In this specification, “(meth) acrylic acid” is used as a generic term for both “acrylic acid” and “methacrylic acid”. Similarly, “(meth) acrylate” is used as a generic term for both “acrylate” and “methacrylate”.

In the polymerization reaction of the copolymer of (meth) acrylic acid polyalkylene glycol monoester and (meth) acrylic acid as described in Patent Document 1 above, together with the polymerization initiator, Chain transfer agents are often added for the purpose of adjusting the degree of polymerization. An example of this chain transfer agent is a relatively inexpensive thiol compound. In the above-mentioned Patent Document 1, it is described that mercaptoethanol is used as an accelerator together with a polymerization initiator, and mercaptoethanol as an accelerator corresponds to a chain transfer agent.

The present inventors have made polyalkylene glycol alkenyl ester / (meth) acrylic acid copolymer or polyalkylene glycol alkenyl ether / (meta) with the addition amount of thiol chain transfer agent reduced to 0 or as much as possible. ) It has been found that when an acrylic acid copolymer is used as a gypsum dispersant, the curing time can be shortened without reducing the fluidity of the gypsum slurry.

The copolymer for gypsum dispersant of the present invention comprises a structural unit derived from the monomer (a) represented by the following general formula (A), and a monomer (b) represented by the following general formula (B). Including a copolymer having a structural unit derived from a copolymer having a weight average molecular weight of 1 to 200,000, and the amount of sulfur element in the copolymer is 0 to 0.2% by weight based on the weight of the copolymer .

Here, the amount of sulfur element in the copolymer is a value determined by the following procedure.

First, ultrafiltration is performed to remove sulfur ionic substances contained in the aqueous copolymer solution, and a measurement sample is prepared. Next, fluorescent X-ray analysis and ion chromatography analysis are performed, respectively, and the amount of sulfur element in the prepared measurement sample is quantified. Using the quantified amount of sulfur element, the amount of sulfur element in the copolymer is calculated by the following mathematical formula.

Amount of sulfur element in copolymer (% by weight) = [(XY) / Z] × 100
here,
X: Amount of sulfur element in the measurement sample quantified by fluorescent X-ray analysis (wt%)
Y: Amount of sulfur element in the measurement sample quantified by ion chromatography analysis (wt%)
Z: Solid content (% by weight) in the measurement sample
It is.

If the amount of elemental sulfur in the copolymer exceeds 0.2% by weight with respect to the copolymer, the curing time of the gypsum slurry becomes longer when the obtained copolymer is used as a dispersant for gypsum. Therefore, it is not preferable. In order to shorten the setting time of the gypsum slurry, the amount of elemental sulfur in the copolymer is preferably 0.17% by weight or less with respect to the copolymer, and is preferably less than 0.1% by weight with respect to the copolymer. It is more preferably 10% by weight or less, and particularly preferably 0.08% by weight or less. Further, the lower limit of the amount of sulfur element in the copolymer is preferably as small as possible, and therefore is substantially preferably 0. However, from the viewpoint of molecular design or production, 0.01% by weight, more preferably 0 It may be set to 0.001% by weight.

In the monomer (a) represented by the general formula (A), the average addition mole number n of the oxyalkylene group is 15 to 200. The lower limit of the average added mole number n is preferably 20. The upper limit of the average added mole number n is preferably 100, more preferably 80. When the average addition mole number n of oxyalkylene groups is less than 15, it is not preferable because the fluidity of the gypsum slurry becomes insufficient when the obtained copolymer is used as a gypsum dispersant. On the other hand, when the average addition mole number n of the oxyalkylene group exceeds 200, it is not preferable because the productivity and production cost of the monomer (a) are inferior.

Examples of the polyalkylene glycol alkenyl ester monomer represented by the general formula (A) include polyethylene glycol mono (meth) acrylate, polypropylene glycol mono (meth) acrylate, polybutylene glycol mono (meth) acrylate, methoxypolyethylene glycol mono ( (Meth) acrylate, methoxypolypropylene glycol mono (meth) acrylate, methoxypolybutylene glycol mono (meth) acrylate, ethoxypolyethylene glycol mono (meth) acrylate, ethoxypolypropylene glycol mono (meth) acrylate, ethoxypolybutylene glycol mono (meth) acrylate , Methoxypolyethylenepolypropylene glycol mono (meth) acrylate, methoxypolyethylenepolypropylene Can be exemplified glycol mono (meth) acrylate, it can be used alone or in combination of two or more thereof.

Examples of the polyalkylene glycol alkenyl ether monomer represented by the general formula (A) include polyethylene glycol-3-methyl-3-butenyl ether, polyethylene glycol-3-butenyl ether, and polyethylene glycol-2-methyl. -2-propenyl ether, polyethylene glycol-3-propenyl ether, polyethylene glycol vinyl ether, polypropylene glycol-3-methyl-3-butenyl ether, polypropylene glycol-3-butenyl ether, polypropylene glycol-2-methyl-2-propenyl Examples include ether, polypropylene glycol-3-propenyl ether, polypropylene glycol vinyl ether, and the like, and one or more of these can be used.

The monomer (a) is preferably an ester represented by the general formula (A) when the value of y is 1.

Examples of the monomer (b) represented by the general formula (B) include (meth) acrylic acid, maleic acid, fumaric acid, itaconic acid, their monovalent metal salts, divalent metal salts, ammonium salts, and Organic amine salts, maleic anhydride, itaconic anhydride and the like can be mentioned, and one or more of these can be used. When a carboxylic acid is used as the monomer (b), the structural unit derived from the monomer (b) is obtained by neutralizing the reaction solution after the polymerization reaction with an alkali, an amine, or the like. Become.

The monomer (b) is preferably a monocarboxylic acid, an alkali metal salt / alkaline earth metal salt / ammonium salt of a monocarboxylic acid, and acrylic acid, methacrylic acid, and an alkali metal salt / alkaline earth metal thereof. More preferred are salts and ammonium salts.

In addition to the monomer (a) represented by the general formula (A) and the monomer (b) represented by the general formula (B), as the monomer (c), styrene, vinyl acetate, hydroxyethyl ( A (meth) acrylate, an alkyl (meth) acrylate, or the like can be used in combination. However, the blending ratio of the monomer (c) is 30% by weight or less of the total of the monomers (a) to (c).

The weight average molecular weight of the copolymer for a gypsum dispersant according to the present invention is 10,000 to 200,000, but it is preferable that the copolymer is also 15,000 to 100,000 within this range.

The copolymer for gypsum dispersant according to the present invention comprises a monomer (a) represented by the general formula (A) and a monomer (b) represented by the general formula (B). It is obtained by adding a polymerization initiator to a body component and copolymerizing it.

The weight ratio of the monomer (a) represented by the general formula (A) and the monomer (b) represented by the general formula (B) is 60:40 to 90 in terms of improving fluidity. : 10 is preferable. If the weight ratio is out of the range, the effect of improving the fluidity of the gypsum slurry by the obtained copolymer is lowered, which is not preferable. In order to obtain a higher fluidity improving effect, the weight ratio of the monomer (a) to the monomer (b) is more preferably 70:30 to 90:10.

Examples of the polymerization initiator include persulfates such as ammonium persulfate, sodium persulfate, and potassium persulfate, hydrogen peroxide, azo compounds such as azobis-2-methylpropionamidine hydrochloride, azobisisobutyronitrile, benzoyl peroxide, Examples include peroxides such as lauroyl peroxide and cumene hydroperoxide. Among these, it is preferable to use a persulfate.

During polymerization, a small amount of a thiol compound that functions as a chain transfer agent may be used in combination with the polymerization initiator. The amount of the thiol compound added during the production of the copolymer is 0 to 1.2 mol%, preferably 0 to 0.7 mol, based on all monomer components including the monomers (a) and (b). Mol%. When the added amount of the thiol compound exceeds 1.2 mol% with respect to the monomer component, it is preferable because the curing time of the gypsum slurry becomes longer when the obtained copolymer is used as a dispersant for gypsum. Absent. In order to shorten the setting time of the gypsum slurry, the addition amount of the thiol compound is preferably 0 to 0.15 mol%, more preferably 0 to 0.1 mol%, more preferably 0 to 0.1 mol% within the above range. 0.05% is particularly preferred.

As the thiol compound used as the chain transfer agent, those represented by the following general formula (C) can be used.

In the formula, R ₇ represents a branched or straight chain alkyl group having 2 to 10 carbon atoms having 1 to 3 carboxyl groups, and a branched or straight chain alkyl group having 1 to 10 carbon atoms having 1 to 3 hydroxyl groups. And a branched or straight chain alkyl group having 1 to 10 carbon atoms having 1 to 3 sulfonic acid groups.

Specific examples of the thiol compound include mercaptoethanol, thioglycerol, thioglycolic acid, 2-mercaptopropionic acid, 3-mercaptopropionic acid, thiomalic acid, octyl thioglycolate, octyl 3-mercaptopropionate, and the like. These 1 type (s) or 2 or more types can be used. Other examples include the thiol compounds described in “POLYMER HANDBOOK Fourth edition, Volume 1, II150 to II157”.

Examples of the solvent for solution polymerization include water, lower alcohols such as methyl alcohol, ethyl alcohol, and 2-propanol, aromatic hydrocarbons such as benzene, toluene, and xylene, and aliphatic carbonization such as cyclohexane and n-hexane. One or two or more of esters such as hydrogen and ethyl acetate; ketones such as acetone and methyl ethyl ketone can be used. Among these, water, methyl alcohol, ethyl alcohol, 2-propanol and the like are particularly preferable.

The copolymer according to the present invention can be used as a constituent of a dispersant for gypsum such as natural gypsum and by-product gypsum. In the present specification, gypsum includes, for example, hemihydrate gypsum, dihydrate gypsum, anhydrous gypsum, phosphate gypsum, hydrofluoric gypsum, and the like.

Moreover, the dispersant for gypsum according to the present invention contains the above-mentioned copolymer. The gypsum composition according to the present invention contains at least gypsum, water, and the above-described copolymer.

The copolymer obtained by the polymerization of the monomers (a) and (b) is not limited to those produced by the production method disclosed in the present specification. It only has to be included. A monomer-derived structural unit corresponds to a structure in which a polymerizable double bond of each monomer is converted to a single bond by a polymerization reaction.

Hereinafter, examples in which the composition for a gypsum dispersant according to the present invention was specifically implemented will be described.

[Examples 1 to 10]
Table 1 shows the monomers (a) and (b) used in Examples and Comparative Examples. Table 2 shows the copolymers according to Examples 1 to 10 and Comparative Examples 1 to 4. In the column of “Constituent components of copolymer” and “Constitutional ratio (weight ratio) of copolymer” in Table 2, it is derived from each monomer after neutralizing the reaction solution with sodium hydroxide. A structural unit and a weight ratio are shown. In addition, “SMAA” in Table 2 means sodium methacrylate.

<Manufacturing method>
The methods for synthesizing the copolymers according to Examples 1 to 10 and Comparative Examples 1 to 4 are as follows.

Example 1
141 parts of water was charged into a glass reaction vessel equipped with a thermometer, a stirrer, a dropping device, a nitrogen inlet tube and a reflux condenser, and nitrogen substitution was performed. After the temperature was raised to 95 ° C. in a nitrogen atmosphere, a single unit for dropping was prepared by mixing 78.4 parts by weight of monomer PGM25E listed in Table 1, 17.6 parts by weight of methacrylic acid (MAA), and 176 parts by weight of water. Two liquids, a meter liquid and 33.7 parts by weight of a 2.3% ammonium persulfate aqueous solution, were dropped simultaneously over 4 hours. Next, 8.4 parts by weight of a 2.3% ammonium persulfate aqueous solution was dropped over 1 hour, and then aged at 95 ° C. for 1 hour. After completion of aging, the copolymer was obtained by adjusting the pH to 7 using a 30% aqueous sodium hydroxide solution.

(Example 2)
141 parts of water was charged into a glass reaction vessel equipped with a thermometer, a stirrer, a dropping device, a nitrogen inlet tube and a reflux condenser, and nitrogen substitution was performed. After raising the temperature to 95 ° C. under a nitrogen atmosphere, 78.4 parts by weight of monomer PGM25E listed in Table 1, 17.6 parts by weight of methacrylic acid, 176 parts by weight of water, 0.03 of β-mercaptopropionic acid Two liquids, a monomer solution for dropping mixed with parts by weight and 33.7 parts by weight of a 4.2% aqueous ammonium persulfate solution, were dropped simultaneously over 4 hours. Next, 8.4 parts by weight of a 4.2% ammonium persulfate aqueous solution was dropped over 1 hour, and then aged at 95 ° C. for 1 hour. After completion of aging, the copolymer was obtained by adjusting the pH to 7 using a 30% aqueous sodium hydroxide solution.

(Example 3)
A copolymer was obtained by the same production method as in Example 2, using 0.02 parts by weight of thiomalic acid instead of β-mercaptopropionic acid.

(Example 4)
A copolymer was obtained by the same production method as in Example 2 using 0.01 parts by weight of thioglycolic acid instead of β-mercaptopropionic acid.

(Example 5)
A copolymer was obtained by the same production method as in Example 2 using 0.01 parts by weight of mercaptoethanol instead of β-mercaptopropionic acid.

(Example 6)
A copolymer was obtained by the same production method as in Example 1, using 70 parts by weight of PGM75E as the monomer (a) and 23.9 parts by weight of methacrylic acid as the monomer (b).

(Example 7)
A copolymer was obtained by the same production method as in Example 2, using 70 parts by weight of PGM75E as the monomer (a) and 23.9 parts by weight of methacrylic acid as the monomer (b).

(Example 8)
A copolymer was obtained by the same production method as in Example 2, using 96 parts by weight of PGM120E as the monomer (a) and 3.2 parts by weight of methacrylic acid as the monomer (b).

Example 9
The monomer (a) was 67 parts by weight of PGM75E, the monomer (b) was 26.3 parts by weight of methacrylic acid, and β-mercaptopropionic acid 0.35 parts by weight. A polymer was obtained.

(Example 10)
The monomer (a) was 67 parts by weight of PGM75E, the monomer (b) was 26.3 parts by weight of methacrylic acid, and 0.41 part by weight of β-mercaptopropionic acid. A polymer was obtained.

(Comparative Example 1)
A copolymer was obtained by the same production method as in Example 2, with the amount of β-mercaptopropionic acid used being 0.41 parts by weight.

(Comparative Example 2)
Example 2 was used with 70 parts by weight of PGM75E as the monomer (a), 23.9 parts by weight of methacrylic acid as the monomer (b), and 0.45 parts by weight of β-mercaptopropionic acid. A copolymer was obtained by the same production method.

(Comparative Example 3)
Example 2 was conducted using 70 parts by weight of PGM75E as the monomer (a), 23.9 parts by weight of methacrylic acid as the monomer (b), and 0.48 parts by weight of β-mercaptopropionic acid. A copolymer was obtained by the same production method.

(Comparative Example 4)
A copolymer was obtained by the same production method as in Example 1, using 80 parts by weight of PGM10E as the monomer (a) and 15.9 parts by weight of methacrylic acid as the monomer (b).

<Adjustment of gypsum slurry>
A gypsum slurry was prepared by charging 264 g of hemihydrate gypsum and 158 g of kneaded water obtained by mixing 0.53 g of any of the above copolymers with water into a small juicer mixer and mixing for 10 seconds.

<Fluidity>
Fill a cone with a bottom diameter of 50 mm and a height of 50 mm with gypsum slurry, lift the cone from a state where the bottom of the cone is pressed on a flat surface, and immediately after that, measure the diameter of the figure formed by spreading the gypsum slurry. The average value was used as the paste flow value. The higher the average value, the better the fluidity.

<Curing property>
The setting time of the gypsum slurry was evaluated based on the start time and the apparent end time measured according to JIS R 9112 using a bigger needle device. More specifically, the initial time and the apparent end time are determined with a bigger needle device using a gypsum slurry poured into a cylindrical plastic container with an inner diameter of 94 mm and a height of 44 mm so that the depth is 38 mm. Measured, and ½ of the sum of the measured start time and apparent end time was taken as the curing time. Here, the starting time is the time from the water injection until the standard needle of the bigger needle device stops at a height of 1 mm from the bottom surface of the co-test body, and the apparent end time is the standard needle of the bigger needle device. Is the time from the water injection until it stops at a height of 1 mm from the surface of the sample. The standard needle of the bigger needle device was 45 mm long and 2 mm in diameter, with its head cut flat. The total mass of what cures with the standard needle is 300 ± 1 g.

Table 3 below shows the flowability and curability test results of the gypsum slurry to which the copolymers according to Examples 1 to 8 and Comparative Examples 1 to 4 were added.

First, in terms of curability, the gypsum slurry to which the copolymers according to Examples 1 to 10 were added had a maximum curing time of 18.6 minutes, and when the copolymers according to Comparative Examples 1 to 4 were added, Compared with, the curing time was shortened. The copolymers according to Comparative Examples 1 to 3 synthesized using a thiol chain transfer agent in an amount exceeding 1.2 mol% with respect to the total amount of the monomers (a) and (b) were added. In the gypsum slurry, the curing time was longer than 30.0 minutes, indicating that the curing time was very long. This is presumably because the increase in the content of thiol-derived sulfur atoms bonded to the copolymer caused inhibition of setting of the gypsum slurry.

Next, regarding the fluidity, the paste flow value of the gypsum slurry to which the copolymers according to Comparative Examples 1 to 4 are added is 190 to 220 mm, whereas the copolymers according to Examples 1 to 8 are added. The paste flow value of the gypsum slurry thus obtained was in the range of 210 to 227 mm, and it was confirmed that there was almost no influence on the fluidity even if the amount of the thiol chain transfer agent was reduced as compared with the conventional case. In addition, although the fluidity | liquidity of the copolymer which concerns on the comparative example 4 is a low value compared with each Example and another comparative example, this is the chain length of the oxyalkylene group of a monomer (a). Is considered to be as short as 10 mol.

[Examples 11 to 14]
Table 4 shows the copolymers according to Examples 11 to 14 and Comparative Example 5. In the columns of “Constituent components of copolymer” and “Constituent ratio (weight ratio) of copolymer” in Table 4, it is derived from each monomer after neutralizing the reaction solution with sodium hydroxide. A structural unit and a weight ratio are shown. Further, “SMA” in Table 4 means sodium maleate.

<Manufacturing method>
The methods for synthesizing the copolymers according to Examples 11 to 14 and Comparative Example 5 are as follows.

(Example 11)
A copolymer was obtained by the same production method as in Example 1, using 67 parts by weight of PGM25E as the monomer (a) and 26.3 parts by weight of methacrylic acid as the monomer (b).

Example 12
The monomer (a) was 67 parts by weight of PGM25E, the monomer (b) was 26.3 parts by weight of methacrylic acid, and 0.27 parts by weight of β-mercaptopropionic acid was used. A polymer was obtained.

(Example 13)
By using 67 parts by weight of PGM25E as the monomer (a), 26.3 parts by weight of methacrylic acid and 0.353 parts by weight of β-mercaptopropionic acid as the monomer (b), the same production method as in Example 2 was used. A polymer was obtained.

(Example 14)
A copolymer was obtained by the same production method as in Example 1, using 82.5 parts by weight of IPN50 as the monomer (a) and 12.7 parts by weight of maleic acid as the monomer (b).

(Comparative Example 5)
The monomer (a) was 75 parts by weight of PGM75E, the monomer (b) was 19.9 parts by weight of methacrylic acid, and 1.0 part by weight of β-mercaptopropionic acid. Coalescence was obtained.

<Method for measuring the amount of sulfur element in the copolymer>
Ultrafiltration was performed to remove sulfur ionic substances in the aqueous copolymer solution obtained by the above synthesis method. As the filtration membrane, an ultrafiltration membrane vivaflow200 (VF20PO) manufactured by Sartorius was connected in parallel. Before the start of filtration, the tube, pump, and filter membrane of the filtration device were filled with ion-exchanged water (74 g of water).

The aqueous copolymer solution prepared to a solid content concentration of 3.0% by weight was placed in a circulation concentration side container, and filtration was started. By filtration, the sulfur ionic substance was removed from the aqueous copolymer solution as a filtrate (waste liquid). As the filtration progressed, the aqueous solution in the circulation concentration side container decreased, so that ion exchange water was added successively so that the weight of the aqueous copolymer solution was 100 g. Filtration was terminated when the total weight of the discharged filtrate reached 260 g.

After completion of filtration, ion exchange water was added to the aqueous copolymer solution in the circulation concentration side container, and the total weight was again adjusted to 100 g. This measurement sample A was subjected to fluorescent X-ray analysis and ion chromatography analysis to quantify the amount of ion elements. A value obtained by subtracting the quantitative value Y (weight%) obtained by ion chromatography analysis from the quantitative value X (weight%) obtained by fluorescent X-ray analysis was defined as the amount of sulfur element introduced into the copolymer.

In addition, PW2404 x-ray spectrometer manufactured by PHILIPS was used for fluorescent X-ray analysis. For ion chromatographic analysis, ICS-3000 (analyzer) manufactured by Dionex, IonPac AS20 (column) manufactured by Dionex, and an aqueous solution (eluent) of 13 to 25 mmol / liter KOH manufactured by Dionex were used.

The solid content Z (% by weight) in the measurement sample A is determined by measuring the weight of the residual solid content obtained by drying the measurement sample A in a nitrogen atmosphere at 130 ° C. for 70 minutes. It was determined as a ratio of the weight of the residual solid content to the weight.

The quantitative values X, Y, and Z obtained as described above were applied to the following mathematical formula to calculate the amount of sulfur element in the copolymer.
Amount of sulfur element in copolymer (% by weight) = [(XY) / Z] × 100

The adjustment of the gypsum slurry and the measurement of fluidity and effectiveness were performed by the same methods as in Examples 1 to 10 and Comparative Examples 1 to 4 described above.

Table 5 below shows the fluidity and curability test results of the gypsum slurry to which the copolymers according to Examples 11 to 14 and Comparative Example 5 were added.

With respect to curability, the gypsum slurry to which the copolymers according to Examples 11 to 14 were added had a maximum curing time of 18.0 minutes, which was higher than that when the copolymer according to Comparative Example 5 was added. Time has been shortened. Thereby, the addition amount of the thiol chain transfer agent is 1.2 mol% or less with respect to the total amount of the monomers (a) and (b), and the amount of elemental sulfur relative to the copolymer weight is 0.2% by weight. % Or less of the copolymers according to Examples 11 to 14 were confirmed to significantly improve the fluidity of the gypsum slurry. On the other hand, the addition amount of the thiol-based chain transfer agent exceeds 1.2 mol% with respect to the total amount of the monomers (a) and (b), and the amount of elemental sulfur relative to the copolymer weight is 0.2 wt%. In the gypsum slurry to which the copolymer according to Comparative Example 5 was added, the curing time was longer than 30.0 minutes, and it was found that the curing time was very long. This is presumably because the increase in the content of thiol-derived sulfur atoms bonded to the copolymer caused inhibition of setting of the gypsum slurry.

Regarding the fluidity, the paste flow values of the copolymers according to Examples 11 to 14 are equivalent to the paste flow value of the gypsum slurry to which the copolymer according to Comparative Example 5 is added, and the thiol chain transfer agent. It was confirmed that there was almost no influence on the fluidity even if the amount of addition was reduced as compared with the conventional case.

From the above results, the amount of the thiol chain transfer agent to be added during the production of the copolymer having the structural unit derived from the monomer (a) and the structural unit derived from the monomer (b) is determined based on the monomer ( By making 1.2 mol% or less with respect to a) and (b), and making the amount of sulfur element contained in the copolymer 0.2 wt% or less, without impairing the fluidity of the gypsum slurry, It was confirmed that a copolymer capable of shortening the setting time of the gypsum slurry was obtained.

The present invention can be used for a gypsum dispersant for improving the dispersibility of gypsum in a gypsum slurry, and a gypsum composition containing gypsum, water, and a preaching dispersant.

Claims

A copolymer for a gypsum dispersant,
It has a structural unit derived from the monomer (a) represented by the following general formula (A) and a structural unit derived from the monomer (b) represented by the following general formula (B), and has a weight average molecular weight. Including a copolymer of 1 to 200,000,
A copolymer for gypsum dispersant, wherein the amount of elemental sulfur in the copolymer is 0.2% by weight or less with respect to the copolymer.

In the formula, R 1 and R 2 are the same or different and represent hydrogen or a methyl group, and AO is the same or different and is one or more types of oxyalkylene groups having 2 or more carbon atoms or two or more types having 2 or more carbon atoms. X represents an integer of 0 to 2, y represents 0 or 1, n is a number of 15 to 200 representing the average number of moles added of the oxyalkylene group, R 3
Represents a hydrogen atom or a hydrocarbon group having 1 to 20 carbon atoms.

In the formula, R 4 , R 5 and R 6 are the same or different and each represents a hydrogen atom, a methyl group or — (CH 2 ) n COOM 2 , and — (CH 2 ) m COOM 2 represents —COOM 1 or other -(CH 2 ) n COOM 2 may form an anhydride, and in this case, M 1 and M 2 of these groups are not present. m represents an integer of 0 to 2, and M 1 and M 2 are the same or different and each represents a hydrogen atom, an alkali metal, an alkaline earth metal, an ammonium group, or an organic ammonium group.
The copolymer for gypsum dispersant according to claim 1, wherein the value of n representing the average added mole number of the oxyalkylene group in the general formula (A) is 15 to 80.
The copolymer for gypsum dispersant according to claim 1, wherein the amount of sulfur element in the copolymer is 0.17% by weight or less with respect to the copolymer.
The copolymer for gypsum dispersant according to claim 1, wherein the monomer (a) is an ester represented by the general formula (A) when the value of y is 1.
The copolymer for gypsum dispersant according to claim 1, wherein the monomer (b) is a monocarboxylic acid or a monocarboxylate.
The copolymer for gypsum dispersant according to claim 5, wherein the monomer (b) is any one of acrylic acid, methacrylic acid, acrylate, and methacrylate.
A method for producing a copolymer for a gypsum dispersant having a weight average molecular weight of 1 to 200,000,
A monomer component containing a monomer (a) represented by the following general formula (A) and a monomer (b) represented by the following general formula (B) is mixed with a polymerization initiator. Polymerization by
The method for producing a copolymer for a gypsum dispersant, wherein the addition amount of the thiol compound added to the monomer component is 1.2 mol% or less with respect to the monomer component.

In the formula, R 1 and R 2 are the same or different and represent hydrogen or a methyl group, and AO is the same or different and is one or more types of oxyalkylene groups having 2 or more carbon atoms or two or more types having 2 or more carbon atoms. X represents an integer of 0 to 2, y represents 0 or 1, n is a number of 15 to 200 representing the average number of moles added of the oxyalkylene group, R 3
Represents a hydrogen atom or a hydrocarbon group having 1 to 20 carbon atoms.

In the formula, R 4 , R 5 and R 6 are the same or different and each represents a hydrogen atom, a methyl group or — (CH 2 ) n COOM 2 , and — (CH 2 ) m COOM 2 represents —COOM 1 or other -(CH 2 ) n COOM 2 may form an anhydride, and in this case, M 1 and M 2 of these groups are not present. m represents an integer of 0 to 2, and M 1 and M 2 are the same or different and each represents a hydrogen atom, an alkali metal, an alkaline earth metal, an ammonium group, or an organic ammonium group.
A method for producing a copolymer for a gypsum dispersant, wherein the amount of the thiol compound added to the monomer component is 0.7 mol% or less with respect to the monomer component.
The method for producing a copolymer for a gypsum dispersant according to claim 7, wherein the monomer (a) is an ester represented by the general formula (A) when the value of y is 1.
The method for producing a copolymer for a gypsum dispersant according to claim 7, wherein the monomer (b) is a monocarboxylic acid or a monocarboxylate.
The method for producing a copolymer for a gypsum dispersant according to claim 10, wherein the monomer (b) is any one of acrylic acid, methacrylic acid, acrylate, and methacrylate.
The method for producing a copolymer for a gypsum dispersant according to claim 3, wherein the value of n representing the average number of added moles of the oxyalkylene group in the general formula (A) is 15 to 80.
The method for producing a copolymer for a gypsum dispersant according to claim 7, wherein the weight ratio of the monomer (a) to the monomer (b) is 60:40 to 90:10.
A gypsum dispersant containing the copolymer for gypsum dispersant according to claim 1.
A gypsum composition comprising gypsum, the copolymer for a dispersant for gypsum according to claim 1, and water.