JP2007113002A - Polymer, manufacturing method of this polymer, and cement admixture by using this polymer - Google Patents

Abstract

<P>PROBLEM TO BE SOLVED: To provide a polymer which contains the constitutional unit derived from a polyoxyalkylene chain and has a specific parameter value and to provide a dispersing agent for inorganic powders, excellent in the dispersion performance. <P>SOLUTION: The polymer (P), containing the constitutional unit derived from a polyoxyalkylene chain and satisfies the range of the PD values defined by the below numerical formula (1). The above numerical formula (1): 1<PD<MD (1) [wherein, PD=Mw/Mn, and MD=G(n)×Mw+H(n)]. <P>COPYRIGHT: (C)2007,JPO&INPIT

Description

  The present invention relates to a polymer, a method for producing the polymer, and a cement admixture using the polymer.

  A polymer having a structural unit derived from a polyoxyalkylene chain is widely used as a dispersant for inorganic powder such as cement as disclosed in Patent Document 1 and Patent Document 2. However, conventional polymers have a wide molecular weight distribution and a large number of high molecular weight parts that aggregate inorganic powder and many low molecular weight parts that do not contribute much to the dispersion performance.

  In particular, in cement dispersants, mortar in which water is added to cement or mortar in which sand, which is fine aggregate, is mixed with coarse paste in mortar. By adding a cement admixture to concrete mixed with stone, the strength and durability of the hardened cement is increased. The cement admixture is required to ensure sufficient dispersibility, fluidity, and workability even when the water content (reduced water) of the cement composition is reduced, and to improve durability and strength by reducing water. Therefore, a cement admixture having high water reduction performance with a small amount added is required.

Among the cement admixtures, polycarboxylic acid type cement admixtures are preferably used because they can impart higher dispersibility to the cement composition than other cement admixtures such as naphthalene. For example, Patent Document 1 discloses a cement admixture including a copolymer composed of a specific unsaturated polyalkylene glycol ester monomer and a (meth) acrylic acid monomer. Patent Document 2 discloses a specific unsaturated polyalkylene glycol ether monomer and a (meth) acrylic acid monomer that is an unsaturated monocarboxylic acid or a maleic acid monomer that is an unsaturated dicarboxylic acid. A cement admixture comprising a copolymer consisting of is disclosed. However, the cement admixture is slightly insufficient in terms of water reduction.
JP-A-9-86990 JP 2001-220417 A

  Under the circumstances described above, the problem to be solved by the present invention is a polymer having a polyalkylene glycol chain and a carboxyl group, but having a very narrow molecular weight distribution different from that of conventional copolymers, and using them. It is to provide a cement admixture with higher dispersibility.

  Although the present inventors show a relatively high cement dispersion performance even with conventional polymers having a wide molecular weight distribution as described in Patent Documents 1 and 2, the high molecular weight portion has an effect of aggregating cement particles. Therefore, the cement dispersion performance was hindered, and the low molecular weight portion was considered not to contribute to the dispersion performance because the cement particle dispersion performance was low. Therefore, a polymer having a narrow molecular weight distribution was created by considering that a polymer having a narrow molecular weight distribution, in which a high molecular weight portion and a low molecular weight portion that do not contribute to the dispersion performance were reduced, would further improve the cement dispersion performance, and the dispersion performance was examined. As a result, a parameter was created based on the obtained result, and the cement composition obtained by using a cement admixture containing a polymer having a parameter value within a specific range has extremely excellent dispersibility. I found out. In that case, it discovered that the polymer which satisfy | fills a parameter could be easily manufactured by carrying out living polymerization of the monomer containing the unsaturated monomer which has a polyoxyalkylene chain, and it came to this invention.

<I> The polymer of the present invention is a polymer (P) containing a structural unit derived from a polyoxyalkylene chain, and satisfies the PD value range defined by the following mathematical formula (1). Coalescence.
1 <PD <MD (1)
[In the formula, PD = Mw / Mn, MD = G (n) × Mw + H (n), G (n) × Mw is the following formula (2)
G (n) × Mw = {− 0.985 × ln (n) +5.802} × 10 ⁻⁵ × Mw (2)
(N represents the average number of moles added of the oxyalkylene group of the polymer (P), and Mw and Mn are respectively weight average molecular weights measured by gel permeation chromatography (GPC) of the polymer (P). Represents the number average molecular weight.)
H (n) is the following formula (3)
H (n) = 4.513 × 10 ⁻⁵ × n ² −6.041 × 10 ⁻³ × n + 1.351 (3)
(N represents the average added mole number of the oxyalkylene group of the polymer (P)). ]

  <Ii> Further, in the polymer, the polymer (P) including the structural unit derived from the polyoxyalkylene chain essentially includes a structural unit having a structural unit derived from the polyoxyalkylene chain and a site derived from a carboxyl group. It is characterized by.

  <Iii> The structural unit derived from the polyoxyalkylene chain of the polymer is represented by the following chemical formula (1):

[Wherein, R ¹ and R ² are the same or different and each represents a hydrogen atom or a methyl group, and AO is the same or different, and one or more of oxyalkylene groups having 2 or more carbon atoms (two or more Or may be added randomly), x represents an integer of 0 to 2, y represents 0 or 1, and n represents an average addition mole of an oxyalkylene group. The number is 1 to 300, and R ³ represents a hydrogen atom or a hydrocarbon group having 1 to 20 carbon atoms]
It is the polymer as described in <i> or <ii> which comprises the structural unit (I) represented by these.

  <Iv> Moreover, the structural unit having the carboxyl group-derived moiety is represented by the following chemical formula (2):

[Wherein, R ⁴ , R ⁵ and R ⁶ are the same or different and are a hydrogen atom or a methyl group, — (CH ₂ ) zCOOM ² (— (CH ₂ ) zCOOM ² is —COOM ¹ or other — (CH _{²⁾ zCOOM 2} and anhydride may form a) represents, Z is an integer of 0 to 2, ^{M 1} and ^{M 2} are the same or different, a hydrogen atom, an alkali metal atom, an alkaline earth metal Represents an atom, an ammonium group or an organic amine group]
It is a polymer as described in <ii> which comprises structural unit (II) represented by these.

  <V> In addition, by conducting living polymerization of an unsaturated monomer (M) including an unsaturated monomer (IM) having a polyoxyalkylene chain, the polyoxyalkylene chain-derived A polymer (P) containing a structural unit can be preferably produced.

  <Vi> At that time, it is also preferred that the unsaturated monomer (M) contains an unsaturated monomer (II-M) having a carboxyl group-derived moiety.

  <Vii> The unsaturated monomer (IM) having the polyoxyalkylene chain is represented by the following chemical formula (3):

[Wherein, R ¹ and R ² are the same or different and each represents a hydrogen atom or a methyl group, and AO is the same or different, and one or more of oxyalkylene groups having 2 or more carbon atoms (two or more Or may be added randomly), x represents an integer of 0 to 2, y represents 0 or 1, and n represents an average addition mole of an oxyalkylene group. The number is 1 to 300, and R ³ represents a hydrogen atom or a hydrocarbon group having 1 to 20 carbon atoms]
It is preferable that it is a manufacturing method as described in <v> which is an unsaturated monomer shown by these.

  <Viii> Moreover, the unsaturated monomer (II-M) having the carboxyl group-derived moiety is represented by the following chemical formula (4).

[Wherein, R ⁴ , R ⁵ and R ⁶ are the same or different and are a hydrogen atom or a methyl group, — (CH ₂ ) zCOOM ² (— (CH ₂ ) zCOOM ² is —COOM ¹ or other — (CH _{²⁾ zCOOM 2} and anhydride may form a) represents, Z is an integer of 0 to 2, ^{M 1} and ^{M 2} are the same or different, a hydrogen atom, an alkali metal atom, an alkaline earth metal Represents a silyl group having an atom, an ammonium group or an organic amine group, or a hydrocarbon group having 3 to 18 carbon atoms]
It is preferable that it is a manufacturing method as described in <vi> which is an unsaturated monomer shown by these.

  The polymer and the polycarboxylic acid polymer for cement admixture of the present invention reduce the high molecular weight side polymer that aggregates the inorganic powder and the low molecular weight side polymer that does not contribute much to cement dispersibility, and have a specific molecular weight distribution. Since the molecular weight distribution is limited to a limited range of parameters, the dispersion performance can be improved by using the polymer as a dispersant for inorganic powder. In particular, when cement is used as the inorganic powder, excellent dispersion performance can be exhibited.

The polymer of the present invention is a polymer (P) containing a structural unit derived from a polyoxyalkylene chain, and the following formula (1)
1 <PD <MD (1)
[In the formula, PD = Mw / Mn, MD = G (n) × Mw + H (n), G (n) × Mw is the following formula (2)
G (n) × Mw = {− 0.985 × ln (n) +5.802} × 10 ⁻⁵ × Mw (2)
(N represents the average number of moles added of the oxyalkylene group of the polymer (P), and Mw and Mn are respectively weight average molecular weights measured by gel permeation chromatography (GPC) of the polymer (P). Represents the number average molecular weight.)
H (n) is the following formula (3)
H (n) = 4.513 × 10 ⁻⁵ × n ² −6.041 × 10 ⁻³ × n + 1.351 (3)
(N represents the average added mole number of the oxyalkylene group of the polymer (P)). ]
It is characterized by satisfying the range of PD values defined by. The MD value can be determined by the following method.

<< Parameter calculation method >>
(1) The weight average molecular weight (Mw) of the polymer (P) containing the structural unit derived from the polyoxyalkylene chain is measured by gel permeation chromatography (GPC).
(2) When the average addition mole number (n) of the oxyalkylene chain of the polymer (P) containing the structural unit derived from the polyoxyalkylene chain is unknown, the average addition mole number (n) is measured by NMR or the like.
(3) The MD value is calculated by substituting the values of the weight average molecular weight (Mw) and the average number of added moles (n) of the oxyalkylene chain obtained in (1) and (2) into the formulas (1) to (3). Ask.

  The MD value is a parameter representing the molecular weight distribution (dispersion degree) of a polymer containing a structural unit derived from a polyoxyalkylene chain. The MD value of the present application will be described below.

Mw / Mn has a strong correlation with Mw. When the polymer has a long side chain such as alkylene glycol, the side chain length (n) also affects Mw / Mn. In the case of copolymers, the composition of the polymer also affects the molecular weight distribution. Therefore, the molecular weight distribution of the copolymer with long side chains is
Mw / Mn = F (Mw, n, composition) (4)
As a function of molecular weight, side chain size, and composition.

  Since GPC measures the relative value in principle, Equation (4) becomes a unique equation under a certain GPC condition, and must be derived from the results of measurement of various polymers under a certain condition so as to be consistent. The derivation of Equation (4) under GPC conditions described later was performed in the following procedure.

As a result of measuring a large number of polymers having different Mw, n, and composition, when the polymer to be measured does not adsorb on the GPC column, the composition has a small influence on the measurement result and can be ignored. MD value) is the following formula (5)
MD = G (n) × Mw + H (n) (5)
It can be expressed as

  The first term on the right side mainly represents the effect of Mw on Mw / Mn, and the second term on the right side represents the effect of polyoxyalkylene chain length n on Mw / Mn.

  For a polymer having a constant oxyalkylene chain length n and different Mw, when Mw is taken on the X axis and Mw / Mn is taken on the Y axis, the relationship between them is expressed by a linear function, and G (n ), And the value of H (n) at that n was calculated from the intercept. For the polymer having another oxyalkylene chain length n, the values of G (n) and H (n) were calculated in the same procedure.

Next, when n is taken on the X axis and G (n) is taken on the Y axis, the relationship between the two is given by the following formula (6).
G (n) = {a1 × ln (n) + a2} × 10 ⁻⁵ (6)
It was well approximated by the natural logarithm shown by. However, a1 and a2 are constants obtained from the measurement results, and are a1 = −0.985 and a2 = 5.802.
Further, when n is taken on the X axis and H (n) is taken on the Y axis, the relationship between the two is given by the following formula (7).
H (n) = b1 × n ² + b2 × n + b3 (7)
It was well approximated by the quadratic equation shown by However, b1, b2, and b3 are constants obtained from the measurement results, and were b1 = 4.513 × 10 ⁻⁵ , b2 = −6.041 × 10 ⁻³ , and b3 = 1.351. Therefore, the formula (6) is expressed by the following formula (8).
MD = {− 0.985 × ln (n) +5.802} × 10 ⁻⁵ × Mw + 4.513 × 10 ⁻⁵ × n ² −6.041 × 10 ⁻³ × n + 1.351 (8)
Indicated by

  The parameter range of the polymer (P) containing the structural unit derived from the polyoxyalkylene chain of the present invention is 1 <PD using the molecular weight distribution (dispersity) parameter value (MD value) obtained from the above formula. <MD range.

  For example, if (a) a polymer having a weight average molecular weight of 30,000 and an average addition mole number of oxyalkylene chain of 25, G (n) × Mw = 0.789, H (n) = 1.226, and molecular weight The distribution parameter value is MD = 0.789 + 1.226 = 2.015. In addition, if (b) a polymer having a weight average molecular weight of 40,000 and an average addition mole number of oxyalkylene chain of 50, G (n) × Mw = 0.799, H (n) = 1.160, and molecular weight The distribution parameter value is MD = 0.799 + 1.160 = 1.939. Accordingly, (a) a polymer having a weight average molecular weight of 30,000 and an average added mole number of oxyalkylene chain of 25 is a polymer having a PD value satisfying PD <2.015. And (b) a polymer having a weight average molecular weight of 40,000 and an average addition mole number of oxyalkylene chain of 50, a polymer having a PD value satisfying PD <1.939 is a polymer of the present invention. (P).

  The above molecular weight distribution parameter value (MD value) is a parameter representing the degree of dispersion (Mw / Mn) of the polymer. A larger value represents a larger degree of dispersion and a wider molecular weight distribution of the polymer. A small value indicates a low degree of dispersion and a narrow molecular weight distribution of the polymer. The polymer (P) of the present invention has a PD value range less than the above molecular weight parameter value (MD value), which means that the molecular weight distribution is very narrow.

  The value of the parameter PD is not particularly limited as long as 1 <PD <MD, but from the viewpoint of improving the dispersion performance of the inorganic powder as the molecular weight distribution (dispersion degree) is narrower, PD <MD-0. 1, more preferably PD <MD-0.15, more preferably PD <MD-0.2, more preferably PD <MD-0.25, more preferably PD <MD-0.3, more preferably PD <MD-0.35. From the viewpoint of polymer production, 1 <PD is preferable, more preferably 1.05 <PD, still more preferably 1.1 <PD, still more preferably 1.15 <PD, and still more preferably 1.2. <PD, more preferably 1.25 <PD, and even more preferably 1.3 <PD.

<Polymer containing structural unit derived from polyoxyalkylene chain>
The polymer (P) containing a structural unit derived from a polyoxyalkylene chain of the present invention is not particularly limited as long as it contains a structural unit derived from a polyoxyalkylene chain in the polymer. A structure grafted on a chain is preferred. The constituent unit derived from the polyoxyalkylene chain is preferably contained in the polymer in an amount of 2 to 98% by mass, more preferably 50% by mass or more, more preferably 60% by mass or more, further preferably 65% by mass or more, and further preferably. It is preferable to contain 70 mass% or more. However, in the calculation of mass%, when the structural unit of the polymer has a functional group capable of forming a salt such as an acid or a base, the mass is calculated in a state where no salt is formed (for example, a carboxylate is a carboxylic acid. In the case of an amine salt, it is converted to an amine), and the same shall apply hereinafter.

  Further, the kind of oxyalkylene group constituting the oxyalkylene chain and the average number of added moles are not particularly limited, but an oxyalkylene group having 2 to 18 carbon atoms is preferable, and an oxyalkylene group having 2 to 8 carbon atoms is more preferable. . Further, from the viewpoint of the dispersion performance of the inorganic powder using water as a medium, it is necessary to increase the hydrophilicity of the oxyalkylene group, and it is preferable that the oxyethylene group having 2 carbon atoms occupies the main component. At this time, the ratio of the oxyethylene group to the total of the oxyalkylene group having 3 or more carbon atoms and the oxyethylene group is 50 mol% or more, preferably 60 mol% or more, more preferably 70 mol% or more, and still more preferably 90 More than mol%, More preferably, it is 95 mol% or more, More preferably, it is 100 mol%.

  Further, the average addition mole number of the oxyalkylene chain is not particularly limited, but the average addition mole number of the oxyalkylene chain is preferably 1 to 300 mol, and preferably 2 mol or more from the viewpoint of improving the dispersion performance of the inorganic powder. Preferably it is 4 mol or more, More preferably, it is 6 mol or more, More preferably, it is 10 mol or more, More preferably, it is 15 mol or more, More preferably, it is 20 mol or more. From the viewpoint of producing an oxyalkylene chain, the upper limit of the oxyalkylene chain is preferably 300 mol, more preferably 250 mol, still more preferably 200 mol, and still more preferably 150 mol.

  The polymer (P) preferably has a structural unit derived from a polyoxyalkylene chain and a structural unit derived from a carboxyl group, and the structural unit having a carboxyl group preferably contains 2 to 90% by mass in the polymer. From the viewpoint of the adsorption performance to the inorganic powder, 2% by mass or more, preferably 5% by mass or more, more preferably 7.5% by mass or more, further preferably 10% by mass or more, more preferably 12.5% by mass or more. More preferably, it is 15% by mass or more, more preferably 20% by mass or more, and further preferably 25% by mass or more. However, if the number of structural units having a carboxyl group is too large, the amount of structural units having a function of dispersing inorganic powder decreases, so the upper limit is 90% by mass, preferably 80% by mass, more preferably 60 mass%, More preferably, it is 50 mass%, More preferably, it is 40 mass%, More preferably, it is 35 mass%, More preferably, it is 30 mass%.

  The structural unit derived from the above polyoxyalkylene chain has the following chemical formula (1)

[Wherein, R ¹ and R ² independently represent a hydrogen atom or a methyl group, and AO independently of each other represents one or a mixture of two or more oxyalkylene groups having 2 or more carbon atoms (two or more Or may be added randomly), x represents an integer of 0 to 2, y represents 0 or 1, and n represents an average addition mole of an oxyalkylene group. The number is 1 to 300, and R ³ represents a hydrogen atom or a hydrocarbon group having 1 to 20 carbon atoms]
It is preferable that 2-98 mass% of structural units (I) represented by these are included. The oxyalkylene chain is preferable because it has a function of dispersing an inorganic powder such as cement particles due to a steric repulsion effect, and the cement particles can be sufficiently dispersed by containing 2 to 98% by mass. In the chemical formula (1), R ¹ and R ² are the same or different and each represents a hydrogen atom or a methyl group, AO is the same or different, and one or a mixture of two or more oxyalkylene groups having 2 or more carbon atoms. (In the case of 2 or more types, it may be added in block form or in random form), x represents an integer of 0 to 2, y represents 0 or 1, and n represents oxyalkylene represents an average addition mole number of groups, the number of 1 to 300, ^{R 3} represents a hydrogen atom or a hydrocarbon group having 1 to 20 carbon atoms.

  In order to obtain the inorganic powder dispersion effect, the structural unit (I) is 2% by mass or more in the polymer (preferably 50% by mass or more, more preferably 60% by mass or more, and further preferably 65% by mass). Or more, more preferably 70% by mass or more). However, if the content of the structural unit (I) increases, the content of the structural unit (II) having a function of adsorbing to inorganic powder particles such as cement decreases, so a large amount of admixture must be added. A composition having sufficient fluidity cannot be obtained. Therefore, the upper limit of the content is 98% by mass (preferably 95% by mass, more preferably 90% by mass, still more preferably 85% by mass, and more preferably 80% by mass).

  In particular, the oxyalkylene group represented by AO is preferably an oxyalkylene group having 2 to 18 carbon atoms, and it is necessary to increase the hydrophilicity of the oxyalkylene group from the viewpoint of improving the dispersion performance of the inorganic powder using water as a medium. It is preferable that the main component is an oxyethylene group which is an oxyalkylene group having 2 carbon atoms. At this time, the ratio of the oxyethylene group to the total of the oxyalkylene group having 3 or more carbon atoms and the oxyethylene group in the structural unit (I) is 50 mol% or more, preferably 60 mol% or more, Preferably it is 70 mol% or more, More preferably, it is 80 mol% or more, More preferably, it is 90 mol% or more, More preferably, it is 100 mol%.

  In addition, by introducing an oxyalkylene group having 3 or more carbon atoms into the oxyalkylene chain in the structural unit (I) and imparting a certain degree of hydrophobicity, the cement particles are provided with a slight structure (network). It is also possible to improve the condition of the concrete produced using the polymer (can reduce the viscosity and stiffness of the concrete). However, if an oxyalkylene group having 3 or more carbon atoms is introduced too much, the hydrophobicity of the obtained polymer becomes too high, so that the performance of dispersing cement may be lowered. From the viewpoint of imparting hydrophobicity, the proportion of the oxyalkylene group having 3 or more carbon atoms in the structural unit (I) is preferably 1 mol% or more, more preferably 3 mol% or more, and even more preferably 5 mol% or more. From the viewpoint of cement dispersion performance, it is preferably 50 mol% or less, more preferably 40 mol% or less, and still more preferably 30 mol% or less.

  From the viewpoint of ease of introduction and affinity with cement, the oxyalkylene group having 3 or more carbon atoms is preferably an oxyalkylene group having 3 to 8 carbon atoms, and further an oxypropylene group or oxybutylene group having 3 to 4 carbon atoms. Is preferred.

  The average number of added moles of the oxyalkylene chain is preferably 1 to 300 moles, preferably 2 moles or more, more preferably 4 moles or more, more preferably 6 moles or more, and still more preferably from the viewpoint of improving the dispersion performance of the inorganic powder. It is 10 mol or more, more preferably 15 mol or more, more preferably 20 mol or more. From the viewpoint of producing an oxyalkylene chain, the upper limit of the oxyalkylene chain is preferably 300 mol, more preferably 250 mol, still more preferably 200 mol, and still more preferably 150 mol.

The terminal group R ³ of the oxyalkylene chain is a hydrogen atom or a hydrocarbon group having 1 to 20 carbon atoms [an alkyl group having 1 to 20 carbon atoms (aliphatic alkyl group or alicyclic alkyl group), alkenyl having 1 to 20 carbon atoms. Group, aromatic group having a benzene ring such as phenyl group, alkylphenyl group and naphthyl group having 1 to 20 carbon atoms, alkynyl group having 1 to 20 carbon atoms, and the like. From the viewpoint of dispersing the powder (cement composition, etc.), it is preferable that the hydrophobicity is low. Furthermore, a hydrogen atom or a hydrocarbon group having 1 to 6 carbon atoms (an alkyl group, an alkenyl group, an alkynyl group, a phenyl group, etc.), further a hydrogen atom or a carbon number 1-3 hydrocarbon groups (an alkyl group, an alkenyl group, an alkynyl group, etc. are mentioned) are preferable.

  The structural unit having the carboxyl group-derived moiety is represented by the following chemical formula (2)

[Wherein R ⁴ , R ⁵ and R ⁶ are each independently a hydrogen atom or a methyl group, — (CH ₂ ) zCOOM ² (— (CH ₂ ) zCOOM ² is —COOM ¹ or other — (CH ₂ Z) may form an anhydride with zCOOM ² ), z represents an integer of 0 to 2, and M ¹ and M ² are each independently a hydrogen atom, an alkali metal atom, an alkaline earth metal atom, Represents an ammonium group or an organic amine group]
It is preferable that 2-90 mass% of structural units (II) represented by these are included.

In the chemical formula (2), R ⁴ , R ⁵ and R ⁶ are the same or different, and are a hydrogen atom or a methyl group, — (CH ₂ ) zCOOM ² (— (CH ₂ ) zCOOM ² is —COOM ¹ or other — (CH ₂ ) may form an anhydride with zCOOM ² ), Z represents an integer of 0 to 2, M ¹ and M ² are the same or different, and are a hydrogen atom, an alkali metal atom, an alkaline earth It represents an analog atom, an ammonium group or an organic amine group.

  The structural unit (II) is a part that exerts an adsorption action on the inorganic powder such as cement, and is 2% by mass or more (preferably 5%) in the polymer from the viewpoint of sufficiently imparting the adsorptivity to the inorganic powder. % By mass or more, more preferably 7.5% by mass or more, more preferably 10% by mass or more, more preferably 12.5% by mass or more, further preferably 15% by mass or more, more preferably 20% by mass or more, and further preferably Is preferably contained in an amount of 25% by mass or more. However, if the content is too high, the content of the structural unit (I) having the function of dispersing the inorganic powder in the polymer is small, so that a composition having sufficient fluidity can be used unless a large amount of admixture is added. Can't get. Therefore, the upper limit of the content is 90% by mass (preferably 80% by mass, more preferably 60% by mass, more preferably 50% by mass, further preferably 40% by mass, more preferably 35% by mass, and further preferably 30% by mass. %).

  The polymer (P) is characterized by having the essential structural unit (repeating unit), and further having a structural unit (III) derived from a monomer (III-M) described later. good. Each of these structural units may be one type or two or more types.

  The ratio of each structural unit constituting the polymer (P) is, by mass ratio, structural unit (I) / structural unit (II) / structural unit (III) = 2 to 98 mass% / 2 to 90 mass%. / 0-50 mass% (preferably 50-95 mass% / 5-80 mass% / 0-40 mass%, more preferably 60-90 mass% / 7.5-60 mass% / 0-30 mass%) It is preferable to use in.

<Monomer for obtaining a polymer (P) containing a structural unit derived from a polyoxyalkylene group>
Examples of the monomer giving the structural unit (I) include the following chemical formula (3)

[Wherein, R ¹ and R ² are the same or different and each represents a hydrogen atom or a methyl group, AO is the same or different, and one or a mixture of two or more oxyalkylene groups having 2 or more carbon atoms (two types In the above case, it may be added in a block form or a random form), x represents an integer of 0 to 2, y represents 0 or 1, and n represents an average of oxyalkylene groups. Represents the number of added moles, is a number from 1 to 300, and R ³ represents a hydrogen atom or a hydrocarbon group having 1 to 20 carbon atoms]
It is represented by an unsaturated monomer component (hereinafter also referred to as “IM”) including a monomer represented by

  As unsaturated monomer component (IM), methanol, ethanol, 1-propanol, 2-propanol, 1-butanol, 2-butanol, 1-pentanol, 1-hexanol, octanol, 2-ethyl-1 -C1-C20 saturated aliphatic alcohols such as hexanol, nonyl alcohol, lauryl alcohol, cetyl alcohol, stearyl alcohol, allyl alcohol, methallyl alcohol, crotyl alcohol, oleyl alcohol, etc. C3-C20 alicyclic alcohols such as saturated aliphatic alcohols, cyclohexanol, phenol, phenylmethanol (benzyl alcohol), methylphenol (cresol), p-ethylphenol, dimethylphenol (xylenol), nonylph Alkoxy polyalkylene glycols obtained by adding an alkylene oxide having 2 to 18 carbon atoms to any of aromatic alcohols having 6 to 20 carbon atoms such as diol, dodecylphenol, phenylphenol and naphthol, Examples include esterified products of polyalkylene glycols obtained by polymerizing 18 alkylene oxides with (meth) acrylic acid and crotonic acid, and one or more of these can be used. Among these, (meth) acrylic acid alkoxypolyalkylene glycol esters are preferred. Further, vinyl alcohol, (meth) allyl alcohol, 3-methyl-3-buten-1-ol, 3-methyl-2-buten-1-ol, 2-methyl-3-buten-2-ol, 2-methyl- The compound which added 1-300 mol of alkylene oxides to unsaturated alcohols, such as 2-buten-1-ol and 2-methyl-3-buten-1-ol, can be mentioned, These 1 type or 2 types or more are used. be able to. Among these monomers, compounds using (meth) allyl alcohol and 3-methyl-3-buten-1-ol are particularly preferable. In addition, said unsaturated ester and unsaturated ether are arbitrary 1 type chosen from C2-C18 alkylene oxides, such as ethylene oxide, propylene oxide, butylene oxide, styrene oxide, as alkylene oxide, Alternatively, two or more alkylene oxides may be added. When two or more types are added, any of random addition, block addition, and alternate addition may be used.

  Examples of the monomer giving the structural unit (II) include the following chemical formula (4)

[Wherein, R ⁴ , R ⁵ and R ⁶ are the same or different and are a hydrogen atom or a methyl group, — (CH ₂ ) zCOOM ² (— (CH ₂ ) zCOOM ² is —COOM ¹ or other — (CH ₂₎ ZCOOM may form a ² and anhydride) represents, Z is an integer of 0 to 2, ^{M 1} and ^{M 2} are the same or different, a hydrogen atom, an alkali metal atom, an alkaline earth atoms Represents a silyl group having an ammonium group, an organic amine group, or a hydrocarbon group having 3 to 18 carbon atoms]
It is represented by an unsaturated monomer component (hereinafter also referred to as “II-M”) including a monomer represented by

  Examples of unsaturated monomers represented by II-M include monocarboxylic acid monomers such as (meth) acrylic acid and crotonic acid, and dicarboxylic acid monomers such as maleic acid, itaconic acid and fumaric acid And anhydrides thereof or salts thereof (for example, salts of monovalent metals, divalent metals, trivalent metals, ammonium, or organic amino acids). Of these, acrylic acid, methacrylic acid, maleic acid, maleic anhydride (in particular, acrylic acid and methacrylic acid are preferred) and salts thereof are preferred from the viewpoint of polymerizability. Two or more of these monomers may be used in combination.

  It is also preferable to further use an unsaturated monomer (III-M) which is a component different from the above-mentioned IM and II-M and is copolymerizable with IM and II-M. As unsaturated monomer III-M, addition of unsaturated dicarboxylic acids such as maleic acid, fumaric acid, itaconic acid, citraconic acid and the like, alkyl alcohols having 1 to 20 carbon atoms, glycols having 2 to 18 carbon atoms or these glycols Monoesters and diesters of a polyalkylene glycol having 2 to 300 moles and an addition of an alkylene oxide having 2 to 18 carbon atoms or an alkylene oxide to an alkyl alcohol having 1 to 20 carbon atoms and an alkoxy polyalkylene oxide having 2 to 300 moles And monoamides of these acids with one-terminal aminated products of alkylamines having 1 to 20 carbon atoms and glycols having 2 to 18 carbon atoms or polyalkylene glycols having 2 to 300 moles of addition of these glycols , Diamides; (meth) acrylic acid Unsaturated monocarboxylic acids such as crotonic acid and alkyl alcohols having 1 to 20 carbon atoms, glycols having 2 to 18 carbon atoms, polyalkylene glycols having 2 to 300 moles of addition of these glycols, and alkyl alcohols having 1 to 20 carbon atoms Or an ester of an alkylene oxide having 2 to 18 carbon atoms or an alkoxypolyalkylene glycol having an addition mole number of alkylene oxide of 2 to 300, or these acids and alkylamines having 1 to 20 carbon atoms and glycols having 2 to 18 carbon atoms Amides with one-terminal amination products of these, or with one-terminal amination products of polyalkylene glycols having an addition mole number of 2 to 300 of these glycols; sulfoethyl (meth) acrylate, 2-methylpropanesulfonic acid (meth) acrylamide, styrene sulfone Acid etc. Unsaturated sulfonic acids, and monovalent metal salts, divalent metal salts, ammonium salts and organic amine salts thereof; unsaturated amides such as (meth) acrylamide and (meth) acrylalkylamide; dimethylaminoethyl (meth) acrylate Unsaturated amino compounds such as; vinyl esters such as vinyl acetate and vinyl propionate; vinyl ethers such as alkyl vinyl ethers having 3 to 20 carbon atoms such as methyl vinyl ether, ethyl vinyl ether, propyl vinyl ether, and butyl vinyl ether; aromatics such as styrene Group vinyls etc. can be mentioned, These 1 type (s) or 2 or more types can be used.

  In order to obtain a polymer by copolymerizing unsaturated monomer (IM), unsaturated monomer (II-M) and unsaturated monomer (III-M), The proportion of use is 100% by mass as the total amount, unsaturated monomer (IM) / unsaturated monomer (II-M) / unsaturated monomer (III-M) = 2 to 98% by mass. / 2-90 mass% / 0-50 mass% (preferably 50-95 mass% / 5-80 mass% / 0-40 mass%, more preferably 60-90 mass% / 7.5-60 mass% / 0 to 30% by mass) is preferable.

  The weight average molecular weight Mw of a polymer (P) can be suitably adjusted according to the objective. For example, in order to use the polymer (P) as a dispersant for the inorganic powder, the Mw of the polymer (P) may be appropriately adjusted depending on the type and particle size of the inorganic powder to be dispersed. When the polymer (P) is used as a cement dispersant, the Mw of the polymer (P) is 1,000 or more from the viewpoint of adsorbing the polymer (P) to the cement particles and sufficiently dispersing the cement particles. Is preferably 5,000 or more, more preferably 10,000 or more, further preferably 15,000 or more, further preferably 20,000 or more, and further preferably 25,000 or more. Further, from the viewpoint of preventing aggregation of cement particles, the Mw of the polymer (P) is preferably 500,000 or less, more preferably 200,000 or less, further preferably 100,000 or less, and further preferably 80,000 or less, 60,000 or less is more preferable, and 40,000 or less is more preferable. However, the value of Mw is the value measured under the GPC conditions described in this specification.

<Manufacture of a polymer (P) containing a structural unit derived from a polyoxyalkylene chain>
The polymer (P) containing the structural unit derived from the polyoxyalkylene chain of the present invention has the parameter value (PD value) of the present invention, and is a polymer characterized by a particularly narrow molecular weight distribution. is there. Examples of the method for producing a polymer having the parameter value (PD value) of the present invention include the following forms.

  (1) A method of fractionating a polymer having a structural unit derived from a polyoxyalkylene chain obtained by a known polymerization method using a gelmerization chromatography (GPC) or a filtration membrane, fractionation based on a difference in solubility, Or dialysis method.

  (2) A method of living polymerizing a monomer containing an unsaturated monomer having a polyoxyalkylene chain. Among living polymerizations, living radical polymerization is preferable. One form of the living radical polymerization method is shown below.

  Many techniques are known for the living radical method. For example, a method using nitrogen oxides such as TEMPO (2,2,6,6-tetramethyl-1-hydroxy), a polymerization method using a transition metal catalyst (ATRP (Atom Transfer Radical Polymerization) method) ), And RAFT (Reversible Addition-Fragmentation chain Transfer) method.

Although it is a polymerization method using a transition element catalyst as a form of living radical polymerization, a highly polar monomer such as a (meth) acrylic monomer or a monomer having a polyalkylene glycol side chain can be obtained by using a novel catalyst system. Are polymerized in a bulk or highly polar solvent. The new catalyst system has the following chemical formula (5)
(M) a (L) b (X) c (5)
[Wherein M is a transition element belonging to the fourth period, L is the following chemical formula (6)
(AI) d (AO) e (AS) f (6)
Wherein AI represents an alkyleneimine, AO represents an alkylene oxide, AS represents an alkylene sulfide, X represents a halogen, and a, b, c, d, e and f each independently represents a number of 0 or more.
And an organic metal compound represented by the following chemical formula (7)

[Wherein R ⁷ , R ⁸ , R ⁹ , R ¹⁰ each independently represents hydrogen, a hydrocarbon group, or a halogen, although the hydrocarbon group may contain one or more halogens or hetero elements. Good]
It is a mixture of the organic halogen compound represented by these.

  The catalyst system is composed of one or more compounds represented by the chemical formula (5) and one or more compounds represented by the chemical formula (7).

  As L in the chemical formula (5), a compound having a heterocyclic ring or an aromatic ring such as a bipyridine compound or a triphenylphosphine compound is generally used, but the solubility in a monomer or a solvent is limited. When a highly polar solvent or highly polar monomer is used, there is a drawback that polymerization does not proceed. On the other hand, the compound of the chemical formula (5) using the compound of the chemical formula (6) contains a large number of nitrogen atoms, oxygen atoms, and sulfur atoms, which have a higher electronegativity compared to the carbon atom, so that even in a highly polar solvent. The stability and solubility were improved, and the affinity for highly polar monomers such as (meth) acrylic monomers and monomers having polyalkylene glycol side chains was increased. As a result, living radical polymerization of highly polar monomers became possible even in a highly polar solvent, and a polymer with a small molecular weight distribution could be obtained in high yield. Moreover, since it is living radical polymerization, unlike conventional radical polymerization, it has become possible to synthesize not only random polymers but also block polymers.

The compound represented by the chemical formula (5) may be used alone or as a mixture of a plurality of compounds satisfying the chemical formula (5). The compound of the chemical formula (5) preferably contains two or more different types of M in order to improve the polymerization rate, and more preferably contains two types of M having different positive charge numbers. In this case, the number of positive charges g, When ^{h (g <h), M} h + molar ratio of relative ^{M g + (M h + /} M g +) is not particularly limited, from the viewpoint of molecular weight distribution, Preferably it is 0.1 mol% or more, more preferably 1 mol% or more, still more preferably 5 mol% or more, further preferably 10 mol% or more, more preferably 20 mol% or more, and from the viewpoint of the polymerization rate. The amount is preferably 1,000 mol% or less, more preferably 200 mol% or less, still more preferably 100 mol% or less, still more preferably 80 mol% or less, and still more preferably 50 mol% or less.

  The molar ratio of the total amount of M to the monomer depends on the molecular weight of the polymer required, but from the viewpoint of the polymerization rate, it is preferably 0.01 mol% or more, more preferably 0.1 mol% or more, More preferably, it is 0.5 mol% or more, further 1 mol% or more, and from the viewpoint of molecular weight distribution, it is preferably 1,000 mol% or less, more preferably 100 mol% or less, and even more preferably 10 mol% or less. More preferably, it is 5 mol% or less.

  M may be one type or a combination of two or more different charges and / or different elements, but a transition element in the fourth period is preferable, and manganese, iron, cobalt, nickel, and copper are more preferably used. It is done.

  The compound of formula (7) must contain one or more halogen atoms. Further, the compound of the chemical formula (7) may be used alone or as a mixture of a plurality of types of compounds satisfying the chemical formula (7). Examples of organic halogen compounds such as chemical formula (7) include halogenated hydrocarbon compounds such as tetrachloromethane, trichloromethane, dichloromethane, monochloroethane, trichlorophenylmethane, dichlorodiphenylmethane, 2,2,2-trichloroacetone, Α-halogenocarbonyl compounds such as 2,2-dichloroacetophenone, methyl 2,2,2-trichloroacetate, methyl 2,2-dichloroacetate, methyl 2-chloropropanoate, ethyl 2-bromo-2-methylpropanoate, 2 -Ethyl iodo-2-methylpropanoate, ethyl 2-bromo-propanoate, ethyl 2-iodo-propanoate, dimethyl 2-chloro-2,4,4-trimethylglutarate, 1,2-bis (2'- Bromo-2′-methylpropionyloxy) ethane, 1,2-bi (2'-bromopropionyl) ethane, may be mentioned 2- (2'-bromo-2'-methyl-propionyloxy) alpha-halogeno-carboxylic acid esters such as ethyl alcohol. These can be used singly or in combination of two or more. Among these, α-halogenocarbonyl compounds and α-halogenocarboxylic acid esters are preferable. Specifically, 2,2-dichloroacetophenone, 2-chloro-2, More preferred are dimethyl 4,4-trimethylglutarate, ethyl 2-bromo-2-methylpropanoate, and ethyl 2-iodo-2-methylpropanoate.

  The molar ratio of the organic halogen compound represented by the chemical formula (7) to the monomer depends on the required molecular weight of the polymer, but is preferably 0.01 mol% or more, more preferably 0, from the viewpoint of the polymerization rate. .1 mol% or more, more preferably 0.5 mol% or more, more preferably 1 mol% or more, and from the viewpoint of molecular weight distribution, preferably 1,000 mol% or less, more preferably 100 mol% or less. More preferably, it is 10 mol% or less, more preferably 5 mol% or less. The content ratio of the compound of the chemical formula (5) and the compound of the chemical formula (7) is not necessarily limited, but the content of the transition element contained in the compound of the chemical formula (5) is the organic halogen compound of the chemical formula (7). The blending molar ratio is not particularly limited, but since the polymerization rate tends to be slow when there are too few transition elements in the chemical formula (5), it is preferably at least 1 mol%, more preferably at least 5 mol%, More preferably, it is 10 mol% or more. On the other hand, if the amount is too large, side reactions are likely to occur, and the molecular weight distribution of the resulting polymer tends to be wide. Therefore, it is preferably 1,000 mol% or less, more preferably 200 mol% or less, and even more preferably 100 mol%. It is as follows.

  The compound represented by the chemical formula (6), that is, a (co) polymer obtained by (co) polymerizing alkyleneimine, alkylene oxide, and alkylene sulfide may be used alone or in combination of two or more. Each of AI, AO, and AS may be used alone or in combination of two or more.

  In the compound represented by the chemical formula (6), d, e, and f represent the number of repeating units of AI, AO, and AS, respectively. From the viewpoint of stabilization of the transition metal element, d is preferably 1 or more, more preferably 2 or more, further preferably 4 or more, more preferably 6 or more, further preferably 10 or more, more preferably 15 or more, From the viewpoint of production, it is preferably 200 or less, more preferably 100 or less, still more preferably 50 or less, and even more preferably 20 or less. From the viewpoint of the solubility of the compound represented by the chemical formula (1), e is preferably 1 or more, more preferably 2 or more, further preferably 3 or more, further preferably 7 or more, more preferably 10 or more, Moreover, from a viewpoint of manufacture, Preferably it is 500 or less, More preferably, it is 300 or less, More preferably, it is 200 or less, More preferably, it is 100 or less, More preferably, it is 50 or less. From the viewpoint of stabilizing the transition metal element, f is preferably 1 or more, more preferably 2 or more, further preferably 4 or more, more preferably 6 or more, still more preferably 10 or more, and still more preferably 15 or more. Moreover, from a viewpoint of manufacture, Preferably it is 200 or less, More preferably, it is 100 or less, More preferably, it is 50 or less, More preferably, it is 20 or less.

  The compound represented by the chemical formula (6) preferably contains two or more of AI, AO, and AS in order to achieve both stability and solubility of the compound represented by the chemical formula (5). It is preferable to contain both AO, and it is further more preferable to consist only of AI and AO. The bonding order of AI, AO, and AS may be a random structure or a block structure, but a block structure is preferable in order to reduce side reactions. A compound obtained by adding AO to active hydrogen of poly AI is more preferable because it is excellent in stability, solubility, and reactivity of the compound represented by the chemical formula (1).

  AI is preferably ethyleneimine from the viewpoints of reactivity and stabilization of transition metal elements. AO is preferably an alkylene oxide having 18 or less carbon atoms, more preferably an alkylene oxide having 8 or less carbon atoms, further preferably an alkylene oxide having 4 or less carbon atoms, and further 3 or less carbon atoms from the viewpoint of reactivity and solubility. More preferred are alkylene oxides, and more preferred are alkylene oxides having 2 carbon atoms. AS is preferably ethylene sulfide from the viewpoints of reactivity and stabilization of transition metal elements.

  The polymer of the present invention is a polymer having a structural unit derived from a polyoxyalkylene chain obtained by the above-mentioned method as an essential component, and in particular, when the polymer of the present invention is used as a cement admixture polymer, The following forms are preferred.

When used as a polymer for cement admixture, it is preferably in the form of an aqueous solution for handling, and other additives may be contained in the cement admixture of the present invention, or the admixture is mixed with cement. In addition, it can also be added. As other additives, known cement additives can be used, for example,
(A) Water-soluble polymer substances: polyacrylic acid (sodium), polymethacrylic acid (sodium), polymaleic acid (sodium), unsaturated carboxylic acid polymer such as sodium salt of acrylic acid / maleic acid copolymer; polyethylene Polyoxyethylene or polyoxypropylene polymers such as glycol and polypropylene glycol or copolymers thereof; Nonionic cellulose ethers such as methylcellulose, ethylcellulose, hydroxymethylcellulose, hydroxyethylcellulose, carboxymethylcellulose, carboxyethylcellulose, hydroxypropylcellulose; yeast glucan Or xanthan gum, β-1,3 glucan (which may be linear or branched, for example, curdlan, paramylon, bakiman, Polysaccharides produced by microbial fermentation such as cleroglucan, laminaran, etc .; polyacrylamide; polyvinyl alcohol; starch; starch phosphate ester; sodium alginate; gelatin; copolymer of acrylic acid having an amino group in its molecule and its quaternary Compounds and the like.

  (A) Polymer emulsion: Copolymers of various vinyl monomers such as alkyl (meth) acrylate.

  (C) retarder: gluconic acid, glucoheptonic acid, alabonic acid, malic acid or citric acid, and oxycarboxylics such as inorganic salts or organic salts such as sodium, potassium, calcium, magnesium, ammonium, triethanolamine, etc. Acids and salts thereof; monosaccharides such as glucose, fructose, galactose, saccharose, xylose, apiose, ribose and isomerized sugar; oligosaccharides such as disaccharides and trisaccharides; oligosaccharides such as dextrin; Sugars, sugars such as molasses containing them; sugar alcohols such as sorbitol; magnesium silicate; phosphoric acid and its salts or boric acid esters; aminocarboxylic acids and their salts; alkali-soluble proteins; humic acids; Phenol; polyhydric alcohol such as glycerine; aminotri ( Tylene phosphonic acid), 1-hydroxyethylidene-1,1-diphosphonic acid, ethylenediaminetetra (methylenephosphonic acid), diethylenetriaminepenta (methylenephosphonic acid) and their alkali metal salts, alkaline earth metal salts and other phosphonic acids and their derivatives etc.

  (D) Early strengthening agents / accelerators: soluble calcium salts such as calcium chloride, calcium nitrite, calcium nitrate, calcium bromide and calcium iodide; chlorides such as iron chloride and magnesium chloride; sulfates; potassium hydroxide; Sodium hydroxide; carbonate; thiosulfate; formate such as formic acid and calcium formate; alkanolamine; alumina cement; calcium aluminate silicate.

(E) Mineral oil-based antifoaming agent: straw oil, liquid paraffin, etc.
(F) Oil-based antifoaming agents: animal and vegetable oils, sesame oil, castor oil, these alkylene oxide adducts, etc.
(G) Fatty acid-based antifoaming agents: oleic acid, stearic acid, and alkylene oxide adducts thereof.
(H) Fatty acid ester antifoaming agent: glycerin monoricinoleate, alkenyl succinic acid derivative, sorbitol monolaurate, sorbitol trioleate, natural wax and the like.

  (U) Oxyalkylene-based antifoaming agent: (Poly) oxyethylene (poly) oxypropylene adduct polyoxyalkylenes; diethylene glycol heptyl ether, polyoxyethylene oleyl ether, polyoxypropylene butyl ether, polyoxyethylene polyoxypropylene (Poly) oxyalkyl ethers such as 2-ethylhexyl ether and oxyethyleneoxypropylene adducts to higher alcohols having 12 to 14 carbon atoms; (poly) oxyalkylenes such as polyoxypropylene phenyl ether and polyoxyethylene nonylphenyl ether (Alkyl) aryl ethers; 2,4,7,9-tetramethyl-5-decyne-4,7-diol, 2,5-dimethyl-3-hexyne-2,5-diol, 3-methyl-1- Spotted Acetylene ethers obtained by addition polymerization of alkylene oxide to acetylene alcohol such as -3-ol; (poly) oxyalkylene fatty acid esters such as diethylene glycol oleate, diethylene glycol laurate, ethylene glycol distearate; polyoxyethylene sorbitan (Poly) oxyalkylene sorbitan fatty acid esters such as monolaurate and polyoxyethylene sorbitan trioleate; (poly) oxyalkylene alkyl (aryl) such as sodium polyoxypropylene methyl ether sulfate and sodium polyoxyethylene dodecylphenol ether sulfate ) Ether sulfate esters; (Poly) oxy such as (poly) oxyethylene stearyl phosphate Ruki alkylene alkyl phosphate esters; polyoxyethylene such as polyoxyethylene lauryl amine (poly) oxyalkylene alkyl amines; polyoxyalkylene amide.

(Co) Alcohol-based antifoaming agent: octyl alcohol, hexadecyl alcohol, acetylene alcohol, glycols and the like.
(Sa) Amide-based antifoaming agent: acrylate polyamine and the like.
(Ii) Phosphate ester antifoaming agent: tributyl phosphate, sodium octyl phosphate, etc.
(S) Metal soap-type antifoaming agents: aluminum stearate, calcium oleate, etc.

  (C) Silicone-based antifoaming agent: dimethyl silicone oil, silicone paste, silicone emulsion, organically modified polysiloxane (polyorganosiloxane such as dimethylpolysiloxane), fluorosilicone oil and the like.

  (So) AE agent: resin soap, saturated or unsaturated fatty acid, sodium hydroxystearate, lauryl sulfate, ABS (alkyl benzene sulfonic acid), LAS (linear alkyl benzene sulfonic acid), alkane sulfonate, polyoxyethylene alkyl (phenyl) ether , Polyoxyethylene alkyl (phenyl) ether sulfate or a salt thereof, polyoxyethylene alkyl (phenyl) ether phosphate or a salt thereof, protein material, alkenyl sulfosuccinic acid, α-olefin sulfonate, and the like.

  (Na) Other surfactants: aliphatic monohydric alcohols having 6 to 30 carbon atoms in the molecule such as octadecyl alcohol and stearyl alcohol, and those having 6 to 30 carbon atoms in the molecule such as abiethyl alcohol Intramolecular such as alicyclic monohydric alcohol, dodecyl mercaptan, etc. Intramolecular such as monovalent mercaptan having 6-30 carbon atoms in the molecule, such as nonylphenol, alkylphenol having 6-30 carbon atoms in the molecule, dodecylamine, etc. 10 mol or more of an alkylene oxide such as ethylene oxide or propylene oxide was added to a carboxylic acid having 6 to 30 carbon atoms in the molecule such as an amine having 6 to 30 carbon atoms, lauric acid or stearic acid. Polyalkylene oxide derivatives; having an alkyl group or an alkoxyl group as a substituent Alkyldiphenyl ether sulfonates in which two phenyl groups having a sulfone group are ether-bonded; various anionic surfactants; various cationic surfactants such as alkylamine acetate and alkyltrimethylammonium chloride; various nonionics Surfactant; various amphoteric surfactants.

(D) Waterproofing agents: fatty acids (salts), fatty acid esters, fats and oils, silicon, paraffin, asphalt, wax, etc.
(Nu) Rust inhibitor: Nitrite, phosphate, zinc oxide and the like.
(E) Crack reducing agent: polyoxyalkyl ethers; alkanediols such as 2-methyl-2,4-pentanediol.
(No) Expansion material: Ettlingite, coal, etc.

  Other known cement additives (materials) include cement wetting agents, thickeners, separation reducing agents, flocculants, drying shrinkage reducing agents, strength enhancers, self-leveling agents, rust preventives, colorants, and antifungal agents. Agents, blast furnace slag, fly ash, cinder ash, clinker ash, husk ash, silica fume, silica powder, gypsum and the like. These known cement additives (materials) may be used alone or in combination of two or more.

  Furthermore, a known cement dispersant can be used in combination with the cement admixture of the present invention. For example, the following can be used.

  Lignin sulfonate; polyol derivative; naphthalene sulfonic acid formalin condensate; melamine sulfonic acid formalin condensate; polystyrene sulfonate; aminoaryl sulfonic acid-phenol-formaldehyde condensate as described in JP-A-1-113419, etc. Aminosulfonic acid type; as described in JP-A-7-267705, as a component (a), a copolymer of a polyalkylene glycol mono (meth) acrylic acid ester compound and a (meth) acrylic acid compound and / or A salt thereof, and as a component (b), a copolymer of a polyalkylene glycol mono (meth) allyl ether compound and maleic anhydride and / or a hydrolyzate thereof, and / or a salt thereof, and a component (c) As polyalkylene glycol mono (meth) allylamine A cement dispersant containing a copolymer of a polyalkylene glycol and a maleic ester of a polyalkylene glycol compound and / or a salt thereof; (meth) acrylic acid as component A as described in Japanese Patent No. 2508113 A copolymer of a polyalkylene glycol ester of (meth) acrylic acid (salt), a specific polyethylene glycol polypropylene glycol compound as the B component, and a concrete admixture comprising a specific surfactant as the C component; (Meth) acrylic acid polyethylene (propylene) glycol ester or polyethylene (propylene) glycol mono (meth) allyl ether, (meth) allyl sulfonic acid (salt), and (meth) as described in JP-A-62-216950 A copolymer comprising acrylic acid (salt). A copolymer comprising polyethylene (propylene) glycol ester of (meth) acrylic acid, (meth) allylsulfonic acid (salt), and (meth) acrylic acid (salt) as described in JP-A-1-226757; As described in JP-B-5-36377, (meth) acrylic acid polyethylene (propylene) glycol ester, (meth) allylsulfonic acid (salt) or p- (meth) allyloxybenzenesulfonic acid (salt), and Copolymer comprising (meth) acrylic acid (salt); copolymer of polyethylene glycol mono (meth) allyl ether and maleic acid (salt) as described in JP-A-4-149056; JP-A-5-170501 (Meth) acrylic acid polyethylene glycol ester, (meth) allylsulfonic acid ( ), (Meth) acrylic acid (salt), alkanediol mono (meth) acrylate, polyalkylene glycol mono (meth) acrylate, and α, β-unsaturated monomer having an amide group in the molecule Polymerization; as described in JP-A-6-191918, polyethylene glycol mono (meth) allyl ether, polyethylene glycol mono (meth) acrylate, (meth) acrylic acid alkyl ester, (meth) acrylic acid (salt), and ( Copolymer comprising meth) allylsulfonic acid (salt) or p- (meth) allyloxybenzenesulfonic acid (salt); alkoxypolyalkylene glycol monoallyl ether and maleic anhydride as described in JP-A-5-43288 Copolymer or its hydrolyzate or its salt; Polyethylene glycol monoallyl ether as described in 58-38380 JP, maleic acid, and copolymers composed of these monomers copolymerizable with monomer, or a salt thereof, or an ester thereof.

  As described in JP-B-59-18338, polyalkylene glycol mono (meth) acrylic acid ester monomer, (meth) acrylic acid monomer, and a monomer copolymerizable with these monomers A copolymer comprising a polymer; a copolymer comprising a (meth) acrylic acid ester having a sulfonic acid group and a monomer copolymerizable therewith as described in JP-A-62-1119147, or Salt thereof; as described in JP-A-6-271347, an esterification reaction product of a copolymer of an alkoxy polyalkylene glycol monoallyl ether and maleic anhydride and a polyoxyalkylene derivative having an alkenyl group at the terminal; Copolymer of alkoxypolyalkylene glycol monoallyl ether and maleic anhydride as described in Kaihei 6-298555 , Esterification reaction product with a polyoxyalkylene derivative having a hydroxyl group at the terminal; as described in JP-A-62-68806, ethylene oxide or the like is added to a specific unsaturated alcohol such as 3-methyl-3-buten-1-ol. Added alkenyl ether monomers, unsaturated carboxylic acid monomers, copolymers consisting of monomers copolymerizable with these monomers, or polycarboxylic acids (salts) such as salts thereof ). These cement dispersants may be used alone or in combination of two or more.

  Other known cement additives (materials) include cement wetting agents, thickeners, separation reducing agents, flocculants, drying shrinkage reducing agents, strength enhancers, self-leveling agents, rust preventives, colorants, and antifungal agents. An agent etc. can be mentioned. These known cement additives (materials) may be used alone or in combination of two or more.

  In the cement composition, the following (1) to (7) may be mentioned as particularly preferred embodiments for components other than cement and water.

  (1) A combination comprising essentially two components, <1> the cement admixture of the present invention and <2> an oxyalkylene-based antifoaming agent. As the oxyalkylene-based antifoaming agent, polyoxyalkylenes, polyoxyalkylene alkyl ethers, polyoxyalkylene acetylene ethers, polyoxyalkylene alkylamines and the like can be used, but polyoxyalkylene alkylamines are particularly preferable. Is preferred. The blending mass ratio of the oxyalkylene antifoaming agent <2> is preferably in the range of 0.01 to 20% by mass with respect to the cement admixture <1>.

  (2) A combination comprising essentially the three components of <1> the cement admixture of the present invention, <2> an oxyalkylene antifoaming agent, and <3> an AE agent. As the oxyalkylene-based antifoaming agent, polyoxyalkylenes, polyoxyalkylene alkyl ethers, polyoxyalkylene acetylene ethers, polyoxyalkylene alkylamines and the like can be used, but polyoxyalkylene alkylamines are particularly preferable. Is preferred. On the other hand, resin acid soaps, alkyl sulfates, and alkyl phosphates are particularly suitable as the AE agent. The blending mass ratio of the cement admixture <1> and the antifoaming agent <2> is preferably 0.01 to 20% by mass with respect to the cement admixture <1>. On the other hand, the blending mass ratio of the AE agent <3> is preferably 0.001 to 2 mass% with respect to the cement.

  (3) <1> the cement admixture of the present invention, <2> a polyalkylene glycol mono (meth) acryl having a polyoxyalkylene chain in which an alkylene oxide having 2 to 18 carbon atoms is added in an average addition mole number of 2 to 300 A copolymer comprising an acid ester monomer, a (meth) acrylic acid monomer and a monomer copolymerizable with these monomers (Japanese Patent Publication No. 59-18338, Japanese Patent Laid-Open No. 7-223852) And 3 components of <3> oxyalkylene-based antifoaming agent are essential. The blending mass ratio of the cement admixture <1> and the copolymer <2> is preferably in the range of 5/95 to 95/5, and more preferably in the range of 10/90 to 90/10. The blending mass ratio of the <3> oxyalkylene-based antifoaming agent is preferably in the range of 0.01 to 20% by mass with respect to the total amount of the cement admixture of <1> and the copolymer of <2>. .

  (4) A combination comprising two components, <1> the cement admixture of the present invention and <2> retarder. As the retarder, oxycarboxylic acids such as gluconic acid (salt) and citric acid (salt), sugars such as glucose, sugar alcohols such as sorbitol, phosphonic acids such as aminotri (methylenephosphonic acid), and the like can be used. . The blending ratio of <1> cement admixture and <2> retarder is the mass ratio of copolymer (A) and / or copolymer (B) to <2> retarder. The range of 50/50 to 99.9 / 0.1 is preferable, and the range of 70/30 to 99/1 is more preferable.

  (5) A combination comprising two components, <1> the cement admixture of the present invention and <2> an accelerator. As the accelerator, soluble calcium salts such as calcium chloride, calcium nitrite and calcium nitrate, chlorides such as iron chloride and magnesium chloride, formates such as thiosulfate, formic acid and calcium formate, and the like can be used. The blending mass ratio of the <1> cement admixture and the <2> accelerator is preferably 10/90 to 99.9 / 0.1, and more preferably 20/80 to 99/1.

  (6) A combination comprising two components, <1> the cement admixture of the present invention and <2> a material separation reducing agent. Examples of the material separation reducing agent include various thickeners such as nonionic cellulose ethers, a hydrophobic substituent composed of a hydrocarbon chain having 4 to 30 carbon atoms as a partial structure, and an alkylene oxide having 2 to 18 carbon atoms. A compound having a polyoxyalkylene chain added in an average addition mole number of 2 to 300 can be used. The blending mass ratio of the cement admixture <1> and the material separation reducing agent <2> is preferably 10/90 to 99.99 / 0.01, and 50/50 to 99.9 / 0. 1 is more preferable. The cement composition of this combination is suitable as high fluidity concrete, self-filling concrete and self-leveling material.

  (7) A combination comprising two components of <1> the cement admixture of the present invention and <2> a sulfonic acid-based dispersant having a sulfonic acid group in the molecule. Examples of the sulfonic acid dispersant include lignin sulfonate, naphthalene sulfonic acid formalin condensate, melamine sulfonic acid formalin condensate, polystyrene sulfonate, aminoaryl sulfonic acid-phenol-formaldehyde condensate and the like. An agent or the like can be used. The mixing ratio of the cement admixture of <1> and the sulfonic acid-based dispersant having a sulfonic acid group in the molecule of <2> is the sulfone in the molecule of <1> and the molecule of <2>. The mass ratio with the sulfonic acid-based dispersant having an acid group is preferably 5/95 to 95/5, more preferably 10/90 to 90/10.

The cement admixture of the present invention can be used in addition to a cement composition such as cement paste, mortar, concrete, etc., similarly to known cement admixtures. It can also be used for ultra high strength concrete. As the cement composition, those usually used including cement, water, fine aggregate, coarse aggregate and the like are suitable. Moreover, what added fine powders, such as a fly ash, blast furnace slag, a silica fume, and a limestone, may be used. Ultra-high-strength concrete is generally called as such in the field of cement composition, that is, the cured product is equivalent to the conventional one even if the water / cement ratio is smaller than that of conventional concrete. Or concrete having a higher strength, for example, the water / cement ratio is 25% by mass or less, further 20% by mass or less, particularly 18% by mass or less, particularly 14% by mass or less, especially about 12% by mass. However, it becomes a concrete having workability that does not hinder normal use, and the cured product thereof is 60 N / mm ² or more, further 80 N / mm ² or more, further 100 N / mm ² or more, particularly 120 N / mm ² or more. , in particular 160 N / mm ² or more, and particularly will exhibit 200 N / mm ² or more compression strength.

As the cement, portland cement such as normal, early strength, super early strength, moderate heat, white, etc .; mixed portland cement such as alumina cement, fly ash cement, blast furnace cement, silica cement and the like are suitable. As the blending amount and unit water amount per 1 m ³ of concrete of the cement, for example, in order to produce highly durable and high strength concrete, the unit water amount is 100 to 185 kg / m ³ , and the water / cement ratio is 10 to 70. % Is preferable. More preferably, the unit water amount is 120 to 175 kg / m ³ and the water / cement ratio is 20 to 65%.

  The added amount ratio of the cement admixture of the present invention in the cement composition is such that the total mass of the polycarboxylic acid polymer (A) and the polycarboxylic acid polymer (B) which are essential components of the present invention is the cement. It is preferable to be 0.01% by mass or more with respect to 100% by mass of the total mass, and it is preferable to be 10% by mass or less. If it is less than 0.01% by mass, the performance may be insufficient, and if it exceeds 10% by mass, the economical efficiency will be inferior. More preferably, they are 0.05 mass% or more and 8 mass% or less, More preferably, they are 0.1 mass% or more and 5 mass% or less. In addition, the said mass% is a value of solid content conversion.

<Molecular weight and molecular weight distribution measurement conditions of copolymer>
Equipment: Waters Alliance (2695)
Analysis software: Empower professional + GPC option column manufactured by Waters: TSKgel guard column (inner diameter 6.0 × 40 mm) + G4000SWXL + G3000SWXL + G2000SWXL (each inner diameter 7.8 × 300 mm)
Detector: differential refractometer (RI) detector (Waters 2414), multi-wavelength visible ultraviolet (PDA) detector (Waters 2996)
Eluent: 115.6 g of sodium acetate trihydrate dissolved in 6001 g of acetonitrile and 10999 g of water, and further adjusted to pH 6.0 with acetic acid Flow rate: 1.0 mL / min Column / Measurement temperature: 40 ° C.
Measurement time: 45 minutes Sample solution injection amount: 100 μL (eluent solution with sample concentration of 0.2-0.5 wt%)
GPC standard sample: Polyethylene glycol manufactured by GL Science Mp = 272500, 219300, 107000, 50000, 24000, 11840, 6450, 4250, 1470 Calibration curve: Created by cubic equation using Mp value of polyethylene glycol Analysis method: In the obtained RI chromatogram, the portions that were flat and stable in the baseline immediately before and after elution of the polymer were connected by straight lines, and the polymer was detected and analyzed. However, when the monomer peak was measured to overlap the polymer peak, the polymer part and the monomer part were separated by vertical division at the most concave part of the overlapping part of the monomer and the polymer, and the molecular weight / molecular weight distribution of only the polymer part was measured. When oligomers higher than dimer were detected, they were included in the polymer part.

<GPC fractionation conditions for copolymer>
Sorting device: HLC-8070 manufactured by Tosoh Corporation
Column: TSKgel α-M + α-2500 (Inside diameter 1 inch, column length 30 cm) manufactured by Tosoh Corporation
Detector: UV detector, 254 nm
Eluent: 50 mM ammonium formate ion exchange aqueous solution / acetonitrile = 85/15 wt% adjusted to pH 8.0 by adding 30% sodium hydroxide Flow rate: 5 mL / min Column / Measurement temperature: 40 ° C.
Sample solution injection amount: 3 mL (eluent solution having a sample concentration of 2 wt%, 18.4 mg / mL)
GPC standard sample: Polyethylene glycol manufactured by Tosoh Corporation Mp = 272500, 219300, 107000, 50000, 24000, 11840, 6450, 4250, 1470 Calibration curve: cubic equation using Mp value of polyethylene glycol Created with.

<Production Example 1: Synthesis of Comparative Polymer 1-1>
A thermometer, a stirrer equipped with a blade having a height of 2.5 cm and a width of 11 cm, a dropping device, a nitrogen introducing tube, and a 3 L glass reactor equipped with a reflux cooling device were charged with 420 g of water and stirred at 200 rpm. The inside of the reactor was heated to 80 ° C. while purging with nitrogen at 100 mL / min. Subsequently, under the same conditions, methoxypolyethylene glycol monomethacrylate (average number of added moles of ethylene oxide 25) 450.319 g, methacrylic acid 89.681 g, 3-mercaptopropionic acid (MPA) 4.511 g, and water 135 g were put in the reactor. The mixed aqueous solution was added dropwise to 6.21 g of ammonium persulfate for 4 hours, and the aqueous solution adjusted to a total of 105 g was dropped into the reactor at a uniform rate over 5 hours. After completion of all the dropwise additions, the polymerization reaction was completed by maintaining the temperature at 80 ° C. for 1 hour, followed by cooling to obtain a comparative polymer 1-1. The obtained polymer was Mw = 24225 and Mw / Mn = 1.928.

<Production Examples 2 to 4: Synthesis of Comparative Polymers 1-2 to 1-4>
In the same procedure as in Production Example 1, only the amount of chain transfer agent (MPA) was changed to obtain comparative polymers having different Mw. Table 1 shows the physical properties of the obtained polymers.

<Production Example 5: Synthesis of Comparative Polymer 2-1>
Thermometer, stirrer with 2.5 cm high and 11 cm wide blade, dripping device, nitrogen inlet tube and 3 L glass reactor equipped with reflux cooling device were charged with 3-methyl-3-butene-1 -Allo ethylene oxide adduct (average number of moles of ethylene oxide added 50) 484.502g, acrylic acid 0.875g, water 250.043g, charged with nitrogen at 100mL / min with stirring at 200rpm, Warmed to 58 ° C. Subsequently, under the same conditions, an aqueous solution adjusted to a total of 38.112 g by adding water to 2.541 g of 30% aqueous hydrogen peroxide was added to the reactor and heated to 58 ° C. Subsequently, with the same conditions, a mixed aqueous solution of 64.623 g of acrylic acid and 61.845 g of water was added for 3 hours to 0.967 g of L-ascorbic acid and 2.141 g of 3-mercaptopropionic acid (MPA) to total 100 g. The aqueous solution prepared in the above was dropped into the reactor at a uniform rate over 3.5 hours. However, the time from the start of heating to the start of dropping was within 2 hours. After completion of the dropwise addition, the polymerization reaction was completed by maintaining the temperature at 58 ° C. for another hour, and then cooled to obtain a comparative polymer 2-1. The obtained polymer was Mw = 36606 and Mw / Mn = 1.978.

<Production Examples 6 to 8: Synthesis of Comparative Polymers 2-2 to 2-4>
In the same procedure as in Production Example 5, only the amount of chain transfer agent (MPA) was changed to obtain comparative polymers having different Mw. The physical properties of the obtained polymer are shown in Table 2, respectively.

<Production Example 9: Synthesis of Comparative Polymer 3-1>
Thermometer, stirrer with 2.5 cm high and 11 cm wide blade, dripping device, nitrogen inlet tube and 3 L glass reactor equipped with reflux cooling device were charged with 3-methyl-3-butene-1 -517.826 g of ethylene oxide adduct (average number of moles of ethylene oxide added 50), 0.935 g of acrylic acid, and 267.241 g of water were charged, and the inside of the reactor was purged with nitrogen at 100 mL / min while stirring at 200 rpm. Warmed to 58 ° C. Subsequently, under the same conditions, an aqueous solution adjusted to a total of 22.879 g by adding water to 1.525 g of 30% hydrogen peroxide solution was added to the reactor and heated to 58 ° C. Subsequently, with the same conditions, a mixed aqueous solution of 31.238 g of acrylic acid and 59.880 g of water was added for 3 hours to 0.592 g of L-ascorbic acid and 1.107 g of 3-mercaptopropionic acid (MPA) to total 100 g. The aqueous solution prepared in the above was dropped into the reactor at a uniform rate over 3.5 hours. However, the time from the start of heating to the start of dropping was within 2 hours. After completion of the dropwise addition, the polymerization reaction was completed by maintaining the temperature at 58 ° C. for an additional hour, followed by cooling to obtain a comparative polymer 3-1. The obtained polymer was Mw = 34965 and Mw / Mn = 1.864.

<Production Examples 10-11: Synthesis of Comparative Polymers 3-2-3-3>
In the same procedure as in Production Example 9, only the amount of chain transfer agent (MPA) was changed to obtain comparative polymers having different Mw. Table 3 shows the physical properties of the obtained polymers.

<Production Examples 12 to 18: Polymers 1-1 to 1-7 of the present invention>
Using the comparative polymer 1-1 synthesized in Production Example 1, GPC fractionation was performed under the above-described conditions until a required amount of polymer was obtained. The obtained 7 fractions were evaporated at 50 ° C. under a reduced pressure of 20 mmHg and concentrated to about 10 wt%. The concentrate was desalted and then evaporated at 50 ° C. under a reduced pressure of 20 mmHg to concentrate to about 10 wt%, and the molecular weight and molecular weight distribution were measured by the methods described above. Preparative conditions and physical properties of the obtained polymer are shown in Table 4.

<Production Examples 19 to 25: Polymers 2-1 to 2-7 of the present invention>
The comparative polymer 2-1 synthesized in Production Example 5 was fractionated by GPC in the same procedure as the method for obtaining the polymers 1-1 to 1-7 of the present invention, and the polymer 2-1 of the present invention was collected. ~ 2-7 was obtained. Preparative conditions and physical properties of the obtained polymer are shown in Table 5.

<Production Examples 26 to 32: Polymers 3-1 to 3-7 of the Present Invention>
In the same procedure as the method for obtaining the polymers 1-1 to 1-7 of the present invention, the comparative polymer 3-1 synthesized in Production Example 9 was fractionated by GPC to obtain the polymer 3-1 of the present invention. ~ 3-7 was obtained. Preparative conditions and physical properties of the obtained polymer are shown in Table 6.

<Production Example 33: Synthesis of catalyst A>
A compound obtained by adding 8 equivalents of ethylene oxide to each active hydrogen of polyethyleneimine (molecular weight 300) (hereinafter referred to as PEIEO, abbreviated as Mw2814) was synthesized by a known method. PEIEO (50.84 g, 1 equivalent) was dissolved in 50.8 g of ion-exchanged water, degassed under reduced pressure at 25 ° C. and 100 mmHg with stirring, and the inside of the system was replaced with nitrogen to return to normal pressure. Under a nitrogen atmosphere, CuBr (4.146 g, 1.6 eq) was added and stirred for 1 hour to obtain aqueous catalyst solution A.

<Production Example 34: Synthesis of catalyst B>
PEIEO (45.34 g, 1 equivalent) was dissolved in 45.3 g of ion-exchanged water, degassed under reduced pressure at 25 ° C. and 100 mmHg with stirring, and the inside of the system was replaced with nitrogen to return to normal pressure. Under a nitrogen atmosphere, CuBr2 (4.678 g, 1.3 eq) was added and stirred for 1 hour to obtain aqueous catalyst solution B.

<Production Example 35: Synthesis of Polymer 4 of the Present Invention>
Catalyst aqueous solution A (1.171 g) prepared in Production Example 33, catalyst aqueous solution B (0.364 g) prepared in Production Example 34, ethyl 2-bromoisobutyrate (0.234 g), and ion-exchanged water (18.829 g) The mixed solution was degassed under reduced pressure at 25 ° C. and 100 mmHg while stirring, and then the atmosphere in the system was replaced with nitrogen to return to normal pressure, whereby catalyst aqueous solution C was obtained. After degassing the mixed aqueous solution of methacrylic acid (2.492 g), methoxypolyethylene glycol monomethacrylate (average EO addition moles 75) (12.508 g), and ion-exchanged water (5 g) at 25 ° C. and 100 mmHg under reduced pressure, The system was replaced with nitrogen to return to normal pressure to obtain an aqueous monomer solution. After the monomer aqueous solution is heated to 50 ° C. in a nitrogen atmosphere, the catalyst aqueous solution C heated to 50 ° C. is added to start the polymerization reaction, and the polymerization reaction is completed by holding the mixture at 50 ° C. for 24 hours with stirring. The polymer 4 was obtained. The obtained polymer was Mw = 35700 and Mw / Mn = 1.40.

<Production Example 36: Synthesis of Polymer 5 of the Present Invention>
Catalyst aqueous solution A (0.878 g) prepared in Production Example 33, catalyst aqueous solution B (0.728 g) prepared in Production Example 34, ethyl 2-bromoisobutyrate (0.117 g), ion-exchanged water (19.122 g) The mixed solution was degassed under reduced pressure at 25 ° C. and 100 mmHg while stirring, and then the atmosphere in the system was replaced with nitrogen to return to normal pressure, whereby catalyst aqueous solution C was obtained. After degassing the mixed aqueous solution of methacrylic acid (2.492 g), methoxypolyethylene glycol monomethacrylate (average EO addition moles 75) (12.508 g), and ion-exchanged water (5 g) at 25 ° C. and 100 mmHg under reduced pressure, The system was replaced with nitrogen to return to normal pressure to obtain an aqueous monomer solution. After the monomer aqueous solution is heated to 50 ° C. in a nitrogen atmosphere, the catalyst aqueous solution C heated to 50 ° C. is added to start the polymerization reaction, and the polymerization reaction is completed by holding the mixture at 50 ° C. for 24 hours with stirring. The polymer 5 was obtained. The obtained polymer was Mw = 30500 and Mw / Mn = 1.36.

<Production Example 37: Synthesis of Comparative Polymer 4>
400 g of water was charged into a 3 L glass reactor having an inner diameter of 16 cm and equipped with a thermometer, a stirrer equipped with a blade having a height of 2.5 cm and a width of 11 cm, a dropping device, a nitrogen introduction tube and a reflux cooling device, and stirred at 200 rpm. The inside of the reactor was heated to 80 ° C. while purging with nitrogen at 100 mL / min. Subsequently, while maintaining the inside of the reactor at 80 ° C., ion-exchanged water was added to 166.785 g of methoxypolyethylene glycol monomethacrylate (average number of moles of ethylene oxide added 75), 33.215 g of methacrylic acid, and 1.592 g of 3-mercaptopropionic acid. In addition, the mixed aqueous solution adjusted to 500 g was added dropwise to the reaction apparatus at a uniform rate for 4 hours, and the aqueous solution prepared by adding ion-exchanged water to 2.292 g of ammonium persulfate to make a total of 100 g was added over 5 hours. After completion of the dropwise addition, the temperature was maintained at 80 ° C. for 1 hour to complete the polymerization reaction, whereby a comparative polymer 4 was obtained. The obtained polymer was Mw = 36400 and Mw / Mn = 1.74.

<Mortar test>
(Contains mortar)
The mortar formulation was C / S / W = 600/600/210 (g). However,
C: Ordinary Portland cement (manufactured by Taiheiyo Cement)
S: Toyoura standard sand W: Sample ion exchange aqueous solution (mortar experimental environment)
The experimental environment was a temperature of 20 ° C. ± 1 ° C. and a relative humidity of 60% ± 10%.

(Mortar kneading procedure)
A predetermined amount of the polymer aqueous solution was weighed, and 10 wt% of the antifoaming agent MA-404 (Pozoris product) was added to the polymer in solid form, and ion-exchanged water was further added to make 210 g, which was sufficiently uniformly dissolved.
A stainless beater (stirring blade) was attached to an N-50 mixer manufactured by HOBART, and a predetermined amount of cement (C) and sand (S) were charged into a kneading container. After kneading at a first speed for 15 seconds, the sample aqueous solution (W) was charged at a constant speed over 15 seconds while kneading. Subsequently, after kneading at a second speed for 30 seconds, the kneading was stopped and the mortar attached to the container wall was scraped off for 15 seconds and left to stand for 45 seconds. The kneading was completed for 90 seconds at the second speed, and the mortar was transferred from the kneading container to a 1 L container made of polyethylene.

(Mortar flow measurement procedure)
The kneaded mortar was immediately stirred 20 times with a spatula and then uniformly packed in a flow cone made of SUS304 having an inner diameter of 55 mm and a height of 50 mm placed on a smooth plate made of SUS304, and the surface was leveled. The flow cone was pulled up vertically, and after the flow of the mortar stopped, the diameter of the spread mortar was measured at two points in length and width, and the average value was taken as the flow value. However, the time from the start of kneading to the measurement of the flow value was kept within 5 minutes and 30 seconds.

(Mortar air volume measurement procedure)
About 200 mL of mortar was packed in a 500 mL Pyrex (registered trademark) graduated cylinder, and rough bubbles were removed by poking with a round bar having a diameter of 8 mm. Furthermore, after adding about 200 mL of mortar and removing bubbles in the same manner, the volume and mass were measured, and the amount of air was calculated from the mass and the density of each material.

<Results of mortar test>
Tables 7 to 10 show the mortar test results of the polymer of the present invention and the comparative polymer.

  Table 7 shows the mortar test results of polymers in which polyalkylene glycol is bonded to the main chain by an ester bond. When comparing the mortar flow values at 0.1 mass% of the added amount of the polymers 1-3 to 1-5 of the present invention having the same weight average molecular weight (Mw) as the comparative polymers 1-1 to 1-4. The comparative polymer is 148 mm to 165 mm, whereas the polymer of the present invention is 207 mm to 220 mm, indicating that the polymer of the present invention is superior in cement dispersion performance. This is because the dispersity (Mw / Mn) of the comparative polymer is 1.61 to 1.93, whereas the dispersity of the polymer of the present invention is 1.36 to 1.38, which is very narrow. It is inferred that this is due to

  Table 8 shows the mortar test results of the polymer in which the polyalkylene glycol chain is bonded to the main chain by an ether bond. When comparing the mortar flow value at the addition amount of 0.1% by mass of the polymer 2-3 to 2-5 of the present invention having the same weight average molecular weight (Mw) as the comparative polymers 2-1 to 2-4. The comparative polymer is 158 mm to 170 mm, whereas the polymer of the present invention is 185 mm to 214 mm, indicating that the polymer of the present invention is superior in cement dispersion performance. This is because the dispersity (Mw / Mn) of the comparative polymer is 1.61 to 1.93, whereas the dispersity of the polymer of the present invention is 1.31 to 1.35, which is very narrow. It is inferred that this is due to This result was the same as the result of the polymer shown in Table 7 in which the polyalkylene glycol chain was bonded to the main chain by an ester bond.

  Table 9 shows the results of a mortar test of a polymer in which the same polyalkylene glycol chain as described above is bonded to the main chain with an ether bond. Similar to the above results, the mortar flow value of the comparative polymer having a dispersity of 1.64 to 1.78 is 154 mm to 177 mm, whereas the weight of the present invention having a dispersity of 1.35 to 1.41 is shown. The polymer of the present invention having a narrow molecular weight distribution with a mortar flow value of 186 mm to 219 mm is superior in cement dispersion performance.

  Table 10 shows the mortar test results of the polymer 4 of the present invention obtained by living radical polymerization and the comparative polymer 4 obtained by conventional radical polymerization. When the mortar flow value is compared with the same addition amount, the comparative polymer 4 obtained by conventional radical polymerization has a mortar flow value of 170 mm, whereas the polymer 4 of the present invention obtained by living radical polymerization has 222 mm. It can be seen that the polymer of the present invention obtained by living radical polymerization is superior in cement dispersion performance. Further, when the degree of dispersion is compared, the polymer of the present invention is 1.40 and the comparative polymer is 1.74, and the molecular weight distribution of the polymer of the present invention is narrower, which is attributed to the dispersion performance. I guess.

<Production Example 38: Synthesis of Polymer 6 of the Present Invention>
A catalyst aqueous solution A (1.098 g) prepared in Production Example 33, a catalyst aqueous solution B (0.910 g) prepared in Production Example 34, ethyl 2-bromoisobutyrate (0.146 g), and ion-exchanged water (17.062 g). The mixed solution was degassed under reduced pressure at 25 ° C. and 100 mmHg with stirring, and then the inside of the system was replaced with nitrogen to return to normal pressure, whereby catalyst aqueous solution C was obtained. While stirring a mixed aqueous solution of methacrylic acid (2.30 g), methoxypolyethylene glycol monomethacrylate (average EO addition mole number 25) (20.20 g), and ion-exchanged water (7.70 g), degassing under reduced pressure at 25 ° C. and 100 mmHg After that, the inside of the system was purged with nitrogen to return to normal pressure to obtain an aqueous monomer solution. After the monomer aqueous solution was heated to 50 ° C. under a nitrogen atmosphere for 24 hours, the catalyst aqueous solution C heated to 50 ° C. was added to start the polymerization reaction, and the polymerization reaction was completed by holding at 50 ° C. for 24 hours with stirring. Inventive polymer 6 was obtained. The obtained polymer was Mw = 26700 and Mw / Mn = 1.64.

<Production Example 39: Synthesis of Polymer 7 of the Present Invention>
Catalyst aqueous solution A (0.878 g) prepared in Production Example 33, catalyst aqueous solution B (0.273 g) prepared in Production Example 34, ethyl 2-bromoisobutyrate (0.176 g), ion-exchanged water (9.90 g) The mixed solution was degassed under reduced pressure at 25 ° C. and 100 mmHg with stirring, and then the inside of the system was replaced with nitrogen to return to normal pressure, whereby catalyst aqueous solution C was obtained. A mixed aqueous solution of methacrylic acid (2.24 g), methoxypolyethylene glycol monomethacrylate (average EO added mole number 25) (11.26 g), and ion-exchanged water (4.69 g) was degassed under reduced pressure at 25 ° C. and 100 mmHg with stirring. After that, the inside of the system was purged with nitrogen to return to normal pressure to obtain an aqueous monomer solution. After the monomer aqueous solution is heated to 50 ° C. in a nitrogen atmosphere, the catalyst aqueous solution C heated to 50 ° C. is added to start the polymerization reaction, and the polymerization reaction is completed by holding at 50 ° C. for 24 hours with stirring. The polymer 7 was obtained. The obtained polymer was Mw = 19000 and Mw / Mn = 1.55.

<Production Example 40: Synthesis of Comparative Polymer 5>
A glass reactor equipped with a thermometer, a stirrer, a dropping device, a nitrogen inlet tube and a reflux cooling device was charged with 1698 g of water, and the temperature inside the reactor was changed to 100 mL / min while stirring at 200 rpm. Warm up. Subsequently, while maintaining the inside of the reaction apparatus at 80 ° C., mixing was performed by adding 500 g of ion-exchanged water to 1796 g of methoxypolyethylene glycol monomethacrylate (average number of added moles of ethylene oxide 25), 204 g of methacrylic acid, and 16.7 g of 3-mercaptopropionic acid. The aqueous solution was dropped into the reaction apparatus at a uniform rate over 230 hours with 10% ammonium persulfate aqueous solution over 4 hours. After completion of all the additions, the polymerization reaction was completed by maintaining the temperature at 80 ° C. for 1 hour to obtain a comparative polymer 5. The obtained polymer was Mw = 22500 and Mw / Mn = 1.76.

<Production Example 41: Synthesis of Comparative Polymer 6>
1700 g of water was charged into a glass reactor equipped with a thermometer, stirrer, dripping device, nitrogen inlet tube and reflux cooling device, and the temperature was increased to 80 ° C. while stirring the reactor at 200 rpm with nitrogen at 100 mL / min. Warm up. Subsequently, with the inside of the reactor kept at 80 ° C., 1580 g of methoxypolyethylene glycol monomethacrylate (average number of moles of ethylene oxide added 25), 420 g of methacrylic acid, 14.5 g of 3-mercaptopropionic acid and 500 g of ion-exchanged water were added. The aqueous solution was dropped into the reaction apparatus at a uniform rate over 230 hours with 10% ammonium persulfate aqueous solution over 4 hours. After completion of all the additions, the polymerization reaction was completed by maintaining the temperature at 80 ° C. for 1 hour to obtain a comparative polymer 6. The obtained polymer was Mw = 25200 and Mw / Mn = 1.89.

<Mortar test>
(Contains mortar)
The mortar formulation was C / S / W = 550/1350/220 (g). However,
C: Ordinary Portland cement (manufactured by Taiheiyo Cement)
S: ISO standard sand (made by Japan Cement Association)
W: Sample ion exchange aqueous solution (mortar experimental environment)
The experimental environment was a temperature of 20 ° C. ± 1 ° C. and a relative humidity of 60% ± 10%.
(Mortar kneading, flow value measurement)
A predetermined amount of the polymer aqueous solution was weighed, and 10 wt% of the antifoaming agent MA-404 (manufactured by Pozoris) was added to the polymer, and further ion-exchanged water was added to make 220 g, which was sufficiently uniformly dissolved.

  For mortar kneading, an N-50 mixer manufactured by HOBART was attached with a stainless beater (stirring blade), and the procedure for kneading and measuring the mortar flow value was in accordance with JIS R5201 (1997). However, the time from the start of kneading to the measurement of the flow value was set within 6 minutes and 30 seconds.

(Measurement of mortar air volume)
About 200 mL of mortar was packed in a 500 mL glass graduated cylinder, struck with a round bar having a diameter of 8 mm, and the container was vibrated to remove coarse bubbles. Furthermore, after adding about 200 mL of mortar and extracting bubbles in the same manner, the volume and mass were measured, and the amount of air was calculated from the mass and the density of each material.

<Results of mortar test>
The mortar test results of the polymer of the present invention and the comparative polymer are shown in Tables 11-12.

  When the mortar flow values of the polymer 6 of the present invention obtained by living radical polymerization and the comparative polymer 5 obtained by conventional radical polymerization are compared, the polymer 6 of the present invention flows at an addition amount of 0.14% by mass. The value is 245 mm, while that of Comparative Polymer 5 is 223 mm. Furthermore, the necessary addition amount for obtaining a flow value equivalent to that of the comparative polymer 5 is 0.12% by mass, and an addition amount of 14% less than that of the comparative polymer 5 may be used. As described above, it can be seen that the polymer obtained by the living radical polymerization of the present invention is superior in cement dispersion performance. Further, comparing the dispersity (Mw / Mn) of the polymer 6 of the present invention and the comparative polymer 5, the polymer 6 of the present invention is 1.64, whereas the comparative polymer 5 is 1.75, indicating that the polymer 6 of the present invention has a narrower molecular weight distribution. The polymer 6 of the present invention has a narrow molecular weight distribution, a high molecular weight portion that aggregates cement, and a low molecular weight portion that does not contribute to cement dispersion performance is reduced. It is thought that the cement dispersion performance was improved because of the increase.

  When the mortar flow values of the polymer 7 of the present invention obtained by living radical polymerization and the comparative polymer 6 obtained by conventional radical polymerization are compared, the polymer 7 of the present invention flows at an addition amount of 0.1% by mass. The value is 252 mm, while that of Comparative Polymer 6 is 210 mm. Furthermore, the necessary addition amount for obtaining a flow value equivalent to that of the comparative polymer 6 is 0.08% by mass, and the addition amount of the comparative polymer 6 may be reduced by 20%. As described above, it can be seen that the polymer obtained by the living radical polymerization of the present invention is superior in cement dispersion performance. Further, comparing the dispersity (Mw / Mn) of the polymer 7 of the present invention and the comparative polymer 6, the polymer 7 of the present invention is 1.55, whereas the comparative polymer 6 is 1.89, indicating that the polymer 7 of the present invention has a narrower molecular weight distribution. The polymer 7 of the present invention has a narrow molecular weight distribution, a high molecular weight part that aggregates cement and a low molecular weight part that does not contribute to cement dispersion performance are reduced, and a molecular weight part that contributes to cement dispersion performance is smaller than that of the comparative polymer 6. It is thought that the cement dispersion performance was improved because of the increase.

Claims (14)

A polymer (P) containing a structural unit derived from a polyoxyalkylene chain, the following formula (1):
1 <PD <MD (1)
[In the formula, PD = Mw / Mn, MD = G (n) × Mw + H (n), G (n) × Mw is the following formula (2):
G (n) × Mw = {− 0.985 × ln (n) +5.802} × 10 ⁻⁵ × Mw (2)
(N represents the average number of moles added of the oxyalkylene group of the polymer (P), and Mw and Mn are the weight average molecular weight and number measured by gel permeation chromatography (GPC) of the polymer (P), respectively. Represents the average molecular weight),
H (n) is the following formula (3):
H (n) = 4.513 × 10 ⁻⁵ × n ² −6.041 × 10 ⁻³ × n + 1.351 (3)
(N represents the average number of moles added of the oxyalkylene group of the polymer (P))]
A polymer satisfying the PD value range defined by The following chemical formula (5):
(M) a (L) b (X) c (5)
[Wherein M is a transition element belonging to the fourth period, and L is the following chemical formula (6):
(AI) d (AO) e (AS) f (6)
Wherein AI represents an alkyleneimine, AO represents an alkylene oxide, AS represents an alkylene sulfide, X represents a halogen, and a, b, c, d, e and f each independently represent a number of 0 or more.
A mixture of an organometallic compound represented by the above and an organic halogen compound.   A polymer (P) containing a structural unit derived from a polyalkylene glycol chain, and comprising the unsaturated polyalkylene glycol monomer (IM) using the mixture according to claim 2 A polymer obtained by polymerizing the body (M).   The polymer according to claim 3, which satisfies the PD value range defined by the mathematical formula (1) according to claim 1.   The polymer according to claim 1, 3 or 4, wherein the polymer (P) containing a structural unit derived from a polyoxyalkylene chain includes a structural unit derived from a polyoxyalkylene chain and a structural unit derived from a carboxyl group. . The structural unit derived from the polyoxyalkylene chain has the following chemical formula (1):

[Wherein, R ¹ and R ² independently represent a hydrogen atom or a methyl group, and AO independently of each other represents one or a mixture of two or more oxyalkylene groups having 2 or more carbon atoms (two or more Or may be added randomly), x represents an integer of 0 to 2, y represents 0 or 1, and n represents an average addition mole of an oxyalkylene group. The number is 1 to 300, and R ³ represents a hydrogen atom or a hydrocarbon group having 1 to 20 carbon atoms]
The polymer of any one of Claim 1 or Claims 3-5 containing the structural unit (I) shown by these. The structural unit having the carboxyl group-derived moiety is represented by the following chemical formula (2):

[Wherein R ⁴ , R ⁵ and R ⁶ are each independently a hydrogen atom or a methyl group, — (CH ₂ ) zCOOM ² (— (CH ₂ ) zCOOM ² is —COOM ¹ or other — (CH ₂ Z) may form an anhydride with zCOOM ² ), z represents an integer of 0 to 2, and M ¹ and M ² are each independently a hydrogen atom, an alkali metal atom, an alkaline earth metal atom, Represents an ammonium group or an organic amine group]
The polymer of Claim 5 containing structural unit (II) shown by these.   A method for producing a polymer (P) containing a structural unit derived from the polyoxyalkylene chain, comprising an unsaturated monomer (M) containing an unsaturated monomer (IM) having a polyoxyalkylene chain. A production method for living polymerization.   The manufacturing method of Claim 8 which carries out living polymerization of the unsaturated monomer (M) containing an unsaturated polyalkylene glycol-type monomer (IM) using the mixture of Claim 2.   The manufacturing method of Claim 8 or 9 in which the said monomer (M) contains the unsaturated monomer (II-M) which has a site | part derived from a carboxyl group. The unsaturated monomer (IM) having the polyoxyalkylene chain is represented by the following chemical formula (3):

[Wherein, R ¹ and R ² independently represent a hydrogen atom or a methyl group, and AO independently of each other represents one or a mixture of two or more oxyalkylene groups having 2 or more carbon atoms (two or more Or may be added randomly), x represents an integer of 0 to 2, y represents 0 or 1, and n represents an average addition mole of an oxyalkylene group. The number is 1 to 300, and R ³ represents a hydrogen atom or a hydrocarbon group having 1 to 20 carbon atoms]
The manufacturing method of Claim 8 or 9 which is an unsaturated monomer shown by these. The unsaturated monomer (II-M) having the carboxyl group-derived moiety is represented by the following chemical formula (4):

[Wherein R ⁴ , R ⁵ and R ⁶ are each independently a hydrogen atom or a methyl group, — (CH ₂ ) zCOOM ² (— (CH ₂ ) zCOOM ² is —COOM ¹ or other — (CH ₂ Z) may form an anhydride with zCOOM ² ), z represents an integer of 0 to 2, and M ¹ and M ² are each independently a hydrogen atom, an alkali metal atom, an alkaline earth metal atom, Represents a silyl group having an ammonium group or an organic amine group, a hydrocarbon group having 1 to 20 carbon atoms, or a hydrocarbon group having 3 to 18 carbon atoms]
The production method according to claim 10, wherein the monomer is an unsaturated monomer.   A cement admixture comprising the polymer according to any one of claims 1 to 7 as an essential component.   The cement admixture which contains the polymer (P) manufactured with the manufacturing method of any one of Claims 8-12 as an essential component.