JP2012229450A - Method for producing acrylic resin - Google Patents

Abstract

PROBLEM TO BE SOLVED: To obtain an acrylic resin having high flowability, processability, impact resistance, solvent resistance, and heat resistance.SOLUTION: The acrylic resin satisfies the following relational expressions (1): 0≤|[(A)-(B)]/(B)|×100(%)≤10 and (2): 0≤|[(C)-(B)]/(B)|×100(%)≤10 when it is sieved by using sieves based on JIS-Z8801, wherein (A) represents a weight-average molecular weight of particles each having a particle diameter of ≥500 μm; (B) represents a weight-average molecular weight of particles each having a particle diameter of 355-300 μm; and (C) represents a weight-average molecular weight of particles each having a particle diameter of ≤150 μm.

Description

  The present invention relates to an acrylic resin, a method for producing an acrylic resin, and a molded body using the acrylic resin.

Methacrylic resins represented by polymethyl methacrylate (PMMA) are widely used in the fields of optical materials, automotive parts, building materials, lenses, household goods, OA equipment, lighting equipment, etc. due to their high transparency. ing. In particular, in recent years, the use for vehicle materials and optical materials such as light guide plates and liquid crystal display films has progressed, and the use of conventional methacrylic resins that makes molding difficult has increased. For example, when injection molding a large and thin molded product, if the fluidity of the resin is poor, the injection pressure is insufficient and molding cannot be performed, or the distortion of the molded product increases. Therefore, a highly fluid resin that can be molded even at a low injection pressure is desired. On the other hand, while maintaining the colorless transparency of the methacrylic resin and the processability of the obtained resin, it is solvent resistant. Further improvement in mechanical strength is also required.
Conventionally, as a known method for improving the mechanical strength and moldability of a methacrylic resin, there is known a method of imparting fluidity with a low molecular weight methacrylic resin and imparting mechanical strength with a high molecular weight or a micro-crosslinked structure. It has been. Relatedly, techniques for melting and mixing high molecular weight or low molecular weight methacrylic resins or expanding the molecular weight distribution using a branched structure have been reported (for example, see Patent Documents 1 to 3).

However, the methacrylic resin described in Patent Document 1 does not satisfy high fluidity and mechanical strength at the same time only by mixing two methacrylic resins having different molecular weights. In addition, since a mixture obtained by separately polymerizing two methacrylic resins having different molecular weights is used by blending, depending on the mixing method, the molecular weight partially varies due to insufficient mixing, and the strand stability during extrusion is reduced. There is a risk of a decrease.
Patent Document 2 describes a technique in which a methacrylic resin constituting a low molecular weight is copolymerized with a large amount of another vinyl monomer copolymerizable with methyl methacrylate. However, the fluidity of the resulting methacrylic resin is not sufficient, and in order to obtain high fluidity, it is necessary to increase the amount of other vinyl monomers copolymerizable with methyl methacrylate. The mechanical properties and mechanical strength tend to decrease, and fluidity, mechanical strength, and heat resistance cannot be imparted in a balanced manner.
Furthermore, in the method for producing a slightly cross-linked methacrylic resin using a polyfunctional monomer described in Patent Document 3, it is very difficult to control the polyfunctional monomer, and a sufficient fluidity imparting effect cannot be obtained. Is insufficient. On the other hand, if the amount of the polyfunctional monomer is excessive, the mixing uniformity is lowered and the appearance of the molded product is lowered. If the amount of the polyfunctional monomer is too small, the improvement of fluidity and the effect of maintaining the mechanical strength cannot be obtained.

  On the other hand, Patent Document 4 discloses a technique for improving fluidity by using a multistage polymerization method while maintaining mechanical strength as compared with a conventional methacrylic resin.

Japanese Patent Publication No. 1-2865 JP-A-4-277545 Japanese Patent Laid-Open No. 9-207196 International Publication No. 2007/060891 Pamphlet

However, although the technology of Patent Document 4 has made it possible to improve the fluidity of the resulting polymer, a deviation in molecular weight occurs between the small particle size and the large particle size, and extrusion and molding operations. In addition, there is a problem that the color tone of the obtained molded piece tends to be lowered.
Further, Patent Document 4 has a problem that polymerization stability is not considered so much, and there is a tendency that agglomerates derived from the fusion of resins and the like tend to increase. When the aggregates increase, the yield decreases, and the productivity is decreased due to clogging due to the clogging of the aggregates in the pipe. Therefore, reduction of the aggregates is required.

  Therefore, in the present invention, an acrylic resin having high fluidity and excellent impact resistance and solvent resistance, and the acrylic resin can be produced without generating aggregates in the production process. It aims at providing the manufacturing method of acrylic resin, and also the molded object using the said acrylic resin.

As a result of intensive studies to solve the above-mentioned problems of the prior art, the present inventors have found that, in particles having a particle size distribution, an acrylic resin having a small variation in molecular weight between particle sizes is the above-mentioned conventional one. The present inventors have found that the above problems can be solved and have completed the present invention.
That is, the present invention is as follows.

[1]
When sieving using a sieve based on JIS-Z8801,
A weight average molecular weight (A) of particles having a particle diameter of 500 μm or more;
A weight average molecular weight (B) of particles having a particle diameter of 355 μm to 300 μm;
A weight average molecular weight (C) of particles having a particle diameter of 150 μm or less;
And an acrylic resin that satisfies the following relational expressions (1) and (2).
0 ≦ | [(A) − (B)] / (B) | × 100 (%) ≦ 10 (1)
0 ≦ | [(C) − (B)] / (B) | × 100 (%) ≦ 10 (2)
[2]
An acrylic resin comprising 80 to 99.5% by mass of methacrylic acid ester monomer units and 0.5 to 20% by mass of other vinyl monomer units copolymerizable with at least one methacrylic acid ester. ,
The weight average molecular weight measured by gel permeation chromatography (GPC) is 60,000 to 300,000,
The acrylic system according to [1], wherein a molecular weight component of 1/5 or less of the peak molecular weight (Mp) obtained from the GPC elution curve is contained in an area area ratio of 7 to 40% obtained from the GPC elution curve. resin.
[3]
The acrylic resin according to [1] or [2], wherein the average particle size is 100 to 500 μm.
[4]
The method for producing an acrylic resin according to any one of [1] to [3],
Using a raw material mixture containing a methacrylic ester, the polymer (I) having a weight average molecular weight of 5,000 to 50,000 measured by gel permeation chromatography is 5 to 45% by mass with respect to the whole acrylic resin. After manufacturing
In the presence of the polymer (I), a polymer (II) having a weight average molecular weight of 60,000 to 350,000 by adding a raw material mixture containing the methacrylic acid ester is 95% of the whole acrylic resin. A step of producing ~ 55% by mass,
The time from the addition of the raw material mixture of the polymer (I) to the arrival of an exothermic peak due to polymerization exotherm is T1,
When the time from the addition of the raw material mixture of the polymer (II) to the peak temperature of the exotherm due to the polymerization exotherm is T2,
The manufacturing method of acrylic resin with which following formula (3) is satisfied.
T2 / T1 ≧ 1 (3)
[5]
The method for producing an acrylic resin according to [4], wherein the following formula (4) is satisfied.
5 ≧ T2 / T1 ≧ 1 (4)
[6]
The method for producing an acrylic resin according to [4] or [5], wherein the T2 is 30 minutes or more and 240 minutes or less.
[7]
Using a raw material mixture containing a methacrylic ester, the polymer (I) having a weight average molecular weight of 5,000 to 50,000 measured by gel permeation chromatography is 5 to 45% by mass with respect to the whole acrylic resin. After manufacturing
In the presence of the polymer (I), a polymer (II) having a weight average molecular weight of 60,000 to 350,000 by adding a raw material mixture containing the methacrylic acid ester is 95% of the whole acrylic resin. A step of producing ~ 55% by mass,
The time from the addition of the raw material mixture of the polymer (I) to the arrival of an exothermic peak due to polymerization exotherm is T1,
When the time from the addition of the raw material mixture of the polymer (II) to the peak temperature of the exotherm due to the polymerization exotherm is T2,
The manufacturing method of acrylic resin with which following formula (3) is satisfied.
T2 / T1 ≧ 1 (3)
[8]
The manufacturing method of the acrylic resin of Claim 7 with which following formula (4) is satisfied.
5 ≧ T2 / T1 ≧ 1 (4)
[9]
The method for producing an acrylic resin according to claim 7 or 8, wherein the T2 is from 30 minutes to 240 minutes.
[10]
An acrylic resin obtained by the production method according to any one of [4] to [9].
[11]
The molded object obtained by shape | molding the acrylic resin as described in said [10].
[12]
The molded product according to [11], which is a vehicle component.

According to the present invention, an acrylic resin having high fluidity, workability, impact resistance, solvent resistance, and heat resistance can be obtained.
Moreover, the production | generation of an aggregate can be suppressed in a superposition | polymerization process, As a result, the manufacturing method of acrylic resin with high productivity can be provided.

It is the schematic of the solvent resistance test by a cantilever method. It is the figure which showed an example of the accumulation area area on a GPC elution curve measurement graph. It is a figure which shows the accumulation area area of the predetermined | prescribed area | region on a GPC elution curve measurement graph. It is a figure which shows the average composition ratio of the high molecular component and low molecular component on the GPC elution curve measurement graph of acrylic resin as an area area.

Hereinafter, a mode for carrying out the present invention (hereinafter referred to as “the present embodiment”) will be described in detail.
The present invention is not limited to the following embodiments, and various modifications can be made within the scope of the gist.
In the present invention, the monomer component before polymerization is referred to as “˜monomer”, and “monomer” may be omitted. Moreover, the structural unit which comprises a polymer is called "-monomer unit."
Hereinafter, in this specification, the acrylic resin is described as including a methacrylic resin.

[Acrylic resin]
(Relationship between particle size and weight average molecular weight)
The acrylic resin of the present embodiment uses a sieve based on JIS-Z8801, and when sieving is performed, the weight average molecular weight (A) of particles having a particle diameter of 500 μm or more, and
A weight average molecular weight (B) of particles having a particle diameter of 355 μm to 300 μm;
A weight average molecular weight (C) of particles having a particle diameter of 150 μm or less;
The following relational expressions (1) and (2) are satisfied.
0 ≦ | [(A) − (B)] / (B) | × 100 (%) ≦ 10 (1)
0 ≦ | [(C) − (B)] / (B) | × 100 (%) ≦ 10 (2)
For the sieving of the fine particles and the method for measuring the weight average molecular weight of each particle, the methods described in Examples described later can be applied.
By satisfying the relationships of the above formulas (1) and (2), an acrylic resin excellent in color tone and workability can be obtained.

(composition)
The acrylic resin of the present embodiment is composed of 80 to 99.5% by mass of methacrylic acid ester monomer units, and 0.5 to 20% by mass of other vinyl monomer units copolymerizable with at least one methacrylic acid ester. % Is preferable.
<Methacrylate monomer>
When the acrylic resin of the present embodiment has the above composition, the methacrylic acid ester monomer constituting this is not particularly limited as long as the effects of the present invention can be achieved. Includes monomers represented by the following general formula (i).

In formula (i), R ₁ represents a methyl group.
R ₂ represents a group having 1 to 12 carbon atoms, preferably a hydrocarbon group having 1 to 12 carbon atoms, and may have a hydroxyl group on the carbon.
Specific examples of suitable methacrylic acid ester monomers include butyl methacrylate, ethyl methacrylate, methyl methacrylate, propyl methacrylate, isopropyl methacrylate, cyclohexyl methacrylate, phenyl methacrylate, methacrylic acid (2-ethylhexyl), Examples thereof include methacrylic acid (t-butylcyclohexyl), benzyl methacrylate, methacrylic acid (2,2,2-trifluoroethyl), and a typical one is methyl methacrylate.
The said methacrylic acid ester monomer may be used individually by 1 type, and may be used in combination of 2 or more type.
In the method for producing an acrylic resin, which will be described later, the “polymer (I)” and the “polymer (II)” may be ones using the same methacrylic acid ester monomer. The acid ester monomer may be used.

<Other vinyl monomers copolymerizable with methacrylic acid ester>
The other vinyl monomer copolymerizable with the methacrylic acid ester is not particularly limited, but an acrylate monomer represented by the following general formula (ii) is preferable. .

R ₃ is a hydrogen atom, and R ₄ is an alkyl group having 1 to 18 carbon atoms.

  Examples of other vinyl monomers copolymerizable with the methacrylic acid ester include α, β-unsaturated acids such as acrylic acid and methacrylic acid; and unsaturated acids such as maleic acid, fumaric acid, itaconic acid, and cinnamic acid. Group-containing divalent carboxylic acids and alkyl esters thereof; styrene, o-methylstyrene, m-methylstyrene, p-methylstyrene, 2,4-dimethylstyrene, 2,5-dimethylstyrene, 3,4-dimethylstyrene, Styrene monomers such as 3,5-dimethylstyrene, p-ethylstyrene, m-ethylstyrene, о-ethylstyrene, p-tert-butylstyrene, isopropenyl benzene (α-methylstyrene); 1-vinylnaphthalene 2-vinylnaphthalene, 1,1-diphenylethylene, isopropenyltoluene, isopropenylethylben Aromatic vinyl compounds such as ethylene, isopropenylpropylbenzene, isopropenylbutylbenzene, isopropenylpentylbenzene, isopropenylhexylbenzene, isopropenyloctylbenzene; Unsaturated carboxylic acid anhydrides such as itaconic acid; N-substituted maleimides such as maleimide, N-methylmaleimide, N-ethylmaleimide, N-phenylmaleimide, and N-cyclohexylmaleimide; Amides such as acrylamide and methacrylamide Ethylene glycol di (meth) acrylate, diethylene glycol di (meth) acrylate, triethylene glycol di (meth) acrylate, tetraethylene glycol di (meth) acrylate Esterylene glycol such as ethylene glycol or its both hydroxyl groups esterified with acrylic acid or methacrylic acid; the hydroxyl groups of two alcohols such as neopentyl glycol di (meth) acrylate and di (meth) acrylate are acrylic acid or methacrylic Examples include those esterified with an acid; those obtained by esterifying a polyhydric alcohol derivative such as trimethylolpropane and pentaerythritol with acrylic acid or methacrylic acid; and polyfunctional monomers such as divinylbenzene.

In addition, in the acrylic resin of the present embodiment, for the purpose of improving particularly required characteristics such as heat resistance, optical characteristics, and workability, a vinyl monomer other than the above-mentioned various materials is appropriately added and copolymerized. You may let them.
For example, from the viewpoint of enhancing light resistance, heat resistance, fluidity, and thermal stability, methyl acrylate, ethyl acrylate, n-propyl acrylate, n-butyl acrylate, sec-butyl acrylate, 2-ethylhexyl acrylate Etc. are preferably used. Methyl acrylate, ethyl acrylate, and n-butyl acrylate are more preferable, and methyl acrylate is easily available, and more preferable.
The said vinylic monomer may be used individually by 1 type, and may be used in combination of 2 or more types.
Further, in the method for producing an acrylic resin to be described later, the “polymer (I)” and the “polymer (II)” may be ones using the same vinyl monomers, and different vinyl types. A monomer may be used.

<Addition amount>
As described above, the acrylic resin of the present embodiment is another vinyl monomer unit copolymerizable with at least one methacrylate ester with respect to 80 to 99.5% by mass of the methacrylate ester monomer unit. It is preferable that 0.5-20 mass% is included, More preferably, it is 0.5-15 mass%, More preferably, it is 0.5-10 mass%, More preferably, it is 0.7-8 mass%, More preferably, it contains 1 to 8% by mass, particularly preferably 1 to 6% by mass.
Thereby, the acrylic resin excellent in fluidity | liquidity, heat resistance, and heat stability is obtained.

(Weight average molecular weight)
The acrylic resin of this embodiment preferably has a weight average molecular weight of 60,000 to 300,000, more preferably 60,000 to 250,000, more preferably 70,000 to 23, as measured by gel permeation chromatography (GPC). More preferably, it is 10,000.
Thereby, an acrylic resin excellent in mechanical strength, solvent resistance, and fluidity can be obtained.
For the measurement of the weight average molecular weight, the elution time and the weight average molecular weight are measured in advance using a monodisperse standard acrylic resin having a known weight average molecular weight and available as a reagent, and an analytical gel column that elutes the high molecular weight component first. From this, a calibration curve is prepared, and the weight average molecular weight of the measurement sample can be obtained from the obtained calibration curve.

  In addition, the molecular weight distribution (weight average molecular weight / number average molecular weight: Mw / Mn) of the acrylic resin of the present embodiment is 2.1 or more and 7 or less from the viewpoint of balance of fluidity, mechanical strength, and solvent resistance. More preferably, it is 2.1 or more and 6 or less, More preferably, it is 2.2 or more and 5 or less, More preferably, it is 2.2 or more and 4.5 or less.

(Peak molecular weight, composition ratio, etc.)
In addition, the acrylic resin of the present embodiment includes a molecular weight component of 1/5 or less of the peak molecular weight (Mp) obtained from the GPC elution curve in an area area ratio of 7 to 40% in the GPC elution curve. It is preferable that it is what is.
Thereby, the improvement of the process fluidity at the time of shaping | molding is achieved, the favorable plasticization effect is acquired, and the distortion suppression of a molded object and the crack suppression effect are acquired.
The content of the molecular weight component of 1/5 or less of the peak molecular weight (Mp) is more preferably 7 to 35%, further preferably 8 to 35%, and still more preferably, in terms of area area ratio in the GPC elution curve. 8-30%.
It should be noted that an acrylic resin having a molecular weight of 500 or less tends to cause a foam-like appearance defect called silver streak at the time of molding.
Here, the peak molecular weight (Mp) refers to the molecular weight showing a peak in the GPC elution curve. When there are a plurality of peaks in the GPC elution curve, it means a peak represented by a molecular weight having the largest abundance.

The content of a molecular weight component equal to or less than 1/5 of the peak molecular weight (Mp) is calculated from the area of the GPC elution curve.
FIG. 2 shows an example of the accumulated area area on the GPC elution curve measurement graph.
The vertical axis of the graph shows RI (differential refraction) detection intensity (mV), the lower part of the horizontal axis of the graph shows elution time (minutes), and the upper part shows the cumulative area area (%) with respect to the entire GPC area area.
In FIG. 2, the area area in the GPC elution curve indicates a hatched portion.
Specifically, first, a base line 7 and a GPC elution curve 6 automatically drawn by a measuring instrument are used for the GPC elution curve obtained from the elution time obtained by GPC measurement and the detected intensity by RI (differential refraction detector). A point A and a point B at which
Point A is a point where the GPC elution curve 6 and the baseline 7 at the beginning of the elution time intersect.
Point B is a position where the molecular weight is 500 or more and the baseline and the GPC elution curve intersect as a rule. When the molecular weight does not intersect within the range of 500 or more, the value of the RI detection intensity at the elution time when the molecular weight is 500 is defined as point B.
A hatched portion surrounded by the GPC elution curve between the points A and B and the line segment AB is an area in the GPC elution curve. The area in the area is the area area in the GPC elution curve. By using the column eluted from the high molecular weight component, the high molecular weight component is observed at the beginning of the elution time, and the low molecular weight component is observed at the end of the elution time.

The cumulative area area (%) of the area area in the GPC elution curve is point 0 shown in FIG. 3 being 0% which is the standard of the cumulative area area (%), and the detection corresponding to each elution time is directed toward the end of the elution time. The view is that the intensity accumulates and an area area in the GPC elution curve is formed.
In FIG. 3, a point on the baseline at a certain elution time is a point X, and a point on the GPC elution curve is a point Y. The ratio of the area surrounded by the curve AY, the line segment AX, and the line segment XY to the total area area in the GPC elution curve is defined as the value of the accumulated area area (%) at a certain elution time.
Hereinafter, using the GPC curve of FIG. 4, the average composition ratio of each component of the high molecular weight component and the low molecular weight component of other vinyl monomer units copolymerizable with the methacrylic acid ester in the acrylic resin. Shown as cumulative area. The average composition ratio of other vinyl monomer units that can be copolymerized with a methacrylic acid ester in an acrylic resin having a cumulative area area of 0 to 2%, that is, a high molecular weight is defined as Mh (mass%). On the other hand, the average composition ratio of other vinyl monomer units that can be copolymerized with a methacrylic ester in an acrylic resin having a cumulative area of 98 to 100%, that is, a low molecular weight is defined as Ml (mass%). FIG. 4 shows a schematic diagram of positions on the graph of the accumulated area area 0 to 2% and the accumulated area area 98 to 100%.

The values of Mh and Ml can be determined by continuously collecting several times or several tens of times according to the column size based on the elution time obtained from GPC.
The composition of the sample collected may be analyzed by a known pyrolysis gas chromatography method.
When the acrylic resin of this embodiment uses a methacrylic ester and a vinyl monomer as polymerization raw materials, the relationship of the following formula (iii) is established between Mh (mass%) and Ml (mass%). It is preferable.
(Mh−0.8) ≧ Ml ≧ 0 (iii)
This indicates that the high molecular weight component has a higher average composition of 0.8% by mass or more of other vinyl monomer units copolymerizable with the methacrylic acid ester than the low molecular weight component. The low molecular weight component indicates that another vinyl monomer is not necessarily copolymerized.
The difference between Mh (mass%) and Ml (mass%) is preferably 0.8 mass% or more, more preferably 1.0 mass% or more for the effect of improving fluidity, and further preferably, That is, equation (iv) holds.
(Mh-2) ≧ Ml ≧ 0 (iv)
That is, by increasing the average composition of the high molecular weight component of other vinyl monomer units copolymerizable with the methacrylic ester of the acrylic resin by 2% by mass or more than the average composition of the low molecular weight component, This is preferable because a dramatic improvement in fluidity can be obtained while maintaining a low incidence of cracks and distortion of the molded product and mechanical strength in environmental tests.

(Average particle size)
The acrylic resin of the present embodiment preferably has an average particle size of 100 to 500 μm. More preferably, it is 150-500 micrometers, More preferably, it is 150-450 micrometers, More preferably, it is 180-450 micrometers, More preferably, it is 200-450 micrometers.
For example, the average particle size is classified using a sieve based on JIS-Z8801, the weight distribution is measured, a particle size distribution is created with the weight distribution, and particles corresponding to 50% by mass from this particle size distribution are prepared. It is obtained by calculating the diameter as the average particle diameter.
Examples of the shape of the acrylic resin particles include a columnar shape, a substantially spherical shape, and a tablet shape, and a substantially spherical shape is preferable from the viewpoint of handleability and uniformity.
When the acrylic resin of this embodiment contains a large amount of fine particles of less than 0.15 mm, it tends to float in the air at the time of handling, and thus the handleability may be deteriorated. In particular, when handling is excellent, it is preferable to reduce the content of such fine particles. However, when all the fine particles of less than 0.15 mm are removed, the number of removal steps increases, leading to an increase in cost, which is allowed to some extent.
From the above viewpoint, the content of the component having a particle size of less than 0.15 mm is preferably 0.01% by mass or more and 10% by mass or less, more preferably 0.1% by mass or more and 10% by mass or less, More preferably, they are 0.1 mass% or more and 8 mass% or less, More preferably, they are 0.2 mass% or more and 7 mass% or less, More preferably, they are 0.3 mass% or more and 6 mass% or less. The content of the component of less than 0.15 mm is a sieve based on JIS-Z8801, JTS-200-45-33 (aperture 500 μm), 34 (aperture 425 μm), 35 (aperture 355 μm), 36 ( Using a sieve tester TSK B-1 with a mesh opening of 300 μm), 37 (aperture 250 μm), 38 (aperture 150 μm), 61 (a saucer), sieved with a vibration force MAX for 10 minutes. Sometimes it is determined by dividing the amount remaining in the pan by the amount screened.

[Method for producing acrylic resin]
Hereinafter, although the manufacturing method of acrylic resin is demonstrated, the manufacturing method of acrylic resin of this embodiment is not limited to the method shown below.
The acrylic resin of this embodiment can be produced by a bulk polymerization method, a solution polymerization method, a suspension polymerization method, or an emulsion polymerization method. A bulk polymerization method, a solution polymerization method and a suspension polymerization method are preferably used, a solution polymerization method and a suspension polymerization method are more preferable, and a suspension polymerization method is more preferably used.
As a specific method for producing the acrylic resin of the present embodiment, for example, the following method may be mentioned.
(First method)
A polymer (I) having a predetermined weight average molecular weight (for example, 5,000 to 50,000) is produced in advance so as to have a predetermined content, and a weight average molecular weight (for example, 6) different from the polymer (I). The polymer (I) is mixed with the raw material composition mixture of the polymer (II) having 10000-350,000). A method in which the mixed solution is polymerized so that the polymer (II) has a predetermined content.
(Second method)
A polymer (I) having a predetermined weight average molecular weight (for example, 5,000 to 50,000) is produced in advance so as to have a predetermined content, and then a weight average molecular weight (for example, different from this polymer (I)) The raw material composition mixture of the polymer (II) having 60,000 to 350,000) is sequentially added to the polymer (I), or the polymer (I) is added to the polymer (II) for each polymer solution (II). ) Is successively added to the raw material composition mixture and polymerized so that the polymer (II) has a predetermined content.

The weight average molecular weight of the polymer (I) is a value measured by gel permeation chromatography from the viewpoint of suppressing occurrence of defects such as silver during molding, ensuring polymerization stability, and imparting fluidity. It is preferable that it is 5,000-50,000 like this, More preferably, it is 10,000-50,000, More preferably, it is 20,000-50,000, More preferably, it is 20,000-35,000.
The weight average molecular weight of the polymer (II) is preferably from 60,000 to 350,000 as described above, more preferably from 70,000 to 320,000, and even more preferably from the viewpoint of mechanical strength and fluidity. 50,000 to 300,000.

In the polymerization step for producing the acrylic resin of this embodiment, a polymerization initiator may be used for the purpose of adjusting the degree of polymerization of the polymer to be produced.
As the polymerization initiator, when performing radical polymerization, di-t-butyl peroxide, lauroyl peroxide, stearyl peroxide, benzoyl peroxide, t-butyl peroxyneodecanate, t-butyl peroxypivalate, Dilauroyl peroxide, dicumyl peroxide, t-butylperoxy-2-ethylhexanoate, 1,1-bis (t-butylperoxy) -3,3,5-trimethylcyclohexane, 1,1-bis Organic peroxides such as (t-butylperoxy) cyclohexane, azobisisobutyronitrile, azobisisovaleronitrile, 1,1-azobis (1-cyclohexanecarbonitrile), 2,2′-azobis-4 -Methoxy-2,4-azobisisobutyronitrile, 2,2'-azobis-2 4-dimethyl valeronitrile, mention may be made of conventional radical polymerization initiator azo such as 2,2'-azobis-2-methylbutyronitrile.
These may be used alone or in combination of two or more.
A combination of these radical initiators and an appropriate reducing agent may be used as a redox initiator.
These initiators are generally used in the range of 0 to 1 part by mass with respect to 100 parts by mass of the total amount of all monomers used, considering the polymerization temperature and the half-life of the initiator. Can be selected as appropriate.
When a bulk polymerization method, a cast polymerization method or a suspension polymerization method is selected, it is possible to prevent coloring of the resin, and so on, so that the peroxide initiators lauroyl peroxide, decanoyl peroxide, and t-butylperoxy- 2-ethylhexanoate and the like can be particularly preferably used, and lauroyl peroxide is particularly preferably used.
In addition, when the solution polymerization method is performed at a high temperature of 90 ° C. or higher, a peroxide, an azobis initiator, or the like that has a 10-hour half-life temperature of 80 ° C. or higher and is soluble in the organic solvent to be used is preferable. Specifically, 1,1-bis (t-butylperoxy) -3,3,5-trimethylcyclohexane, cyclohexane peroxide, 2,5-dimethyl-2,5-di (benzoylperoxy) hexane, , 1-azobis (1-cyclohexanecarbonitrile), 2- (carbamoylazo) isobutyronitrile and the like.
These initiators are preferably used, for example, in the range of 0 to 1 part by mass with respect to 100 parts by mass of the total amount of all monomers used.

In the polymerization step for producing the acrylic resin of this embodiment, the molecular weight of the polymer to be produced can be controlled.
For example, the molecular weight can be controlled by using chain transfer agents such as alkyl mercaptans, dimethylacetamide, dimethylformamide and triethylamine, and iniferters such as dithiocarbamates, triphenylmethylazobenzene and tetraphenylethane derivatives.
The molecular weight can be adjusted by adjusting the amount of these additives.
When these additives are used, alkyl mercaptans are preferably used from the viewpoint of handleability and stability. For example, n-butyl mercaptan, n-octyl mercaptan, n-dodecyl mercaptan, t-dodecyl mercaptan, n-tetra Examples include decyl mercaptan, n-octadecyl mercaptan, 2-ethylhexyl thioglycolate, ethylene glycol dithioglycolate, trimethylolpropane tris (thioglycolate), pentaerythritol tetrakis (thioglycolate) and the like.
These can be appropriately added according to the required molecular weight, but generally used in the range of 0.001 to 3 parts by mass with respect to 100 parts by mass of the total amount of all monomers used. .
Other molecular weight control methods include a method of changing the polymerization method, a method of adjusting the amount of the polymerization initiator, and a method of changing the polymerization temperature.
These molecular weight control methods may be used alone, or two or more methods may be used in combination.

  The polymerization temperature may be appropriately selected depending on the polymerization method, and is preferably 50 ° C. or higher and 200 ° C. or lower. The relationship between the polymerization temperature and the holding time in the case of producing an acrylic resin by applying the above (first method) and (second method) will be described later.

  The above-described method is a method for producing an acrylic resin containing two types of polymer (I) and polymer (II) components having different weight average molecular weights. However, the present invention is not limited to this example, and an acrylic resin containing polymers having different weight average molecular weights may be produced by the same operation.

The method for producing the polymer (II) in the state where the polymer (I) is produced and the polymer (I) is present in the raw material composition mixture of the polymer (II) is the present embodiment. This is a preferable method for producing the acrylic resin.
This method is preferable because the compositions of the polymer (I) and the polymer (II) can be easily controlled, the temperature rise due to heat generated during polymerization can be suppressed, and the viscosity in the system can be stabilized.
In this case, the raw material composition mixture of the polymer (II) may be in a state where the polymerization is partially started. As a polymerization method therefor, any one of bulk polymerization, solution polymerization, suspension polymerization, or emulsion polymerization is preferable, and bulk polymerization, solution polymerization, and suspension polymerization are more preferable.

<Blending ratio of polymers (I) and (II)>
Next, regarding the method for producing the acrylic resin, specific blending ratios of the above-described polymers (I) and (II) will be described.
In the following description, the polymers (I) and (II) are both methacrylic acid ester-based polymers containing a methacrylic acid ester monomer as a polymerization raw material.
In both the above (first method) and (second method), the methacrylic acid ester monomer, or the methacrylic acid ester monomer and at least one kind of methacrylic acid ester are combined in the first stage polymerization step. By polymerizing another polymerizable vinyl monomer, a methacrylic acid ester polymer (polymer (I)) is obtained. In the second stage polymerization step, the methacrylic acid ester monomer or the methacrylic acid ester monomer And a methacrylic ester polymer (polymer (II)) obtained by polymerizing another vinyl monomer copolymerizable with at least one methacrylic ester.
These compounding ratios are polymer (I): 5-45 mass%, and it is preferable that it is polymer (II): 95-55 mass%.
By setting it as such a compounding ratio, the polymerization stability in a manufacturing process can be aimed at, and it is preferable also from a viewpoint of the fluidity | liquidity of a methacrylic resin, a moldability, and mechanical strength. In order to further improve the balance of these characteristics, the ratio of polymer (I) / polymer (II) is more preferably 5 to 40% by mass / 95 to 60% by mass, and more preferably 5 to 35% by mass. % / 95 to 65% by mass is more preferable, and 10 to 35% by mass / 90 to 65% by mass is even more preferable.

As a raw material for the polymer (I), when other vinyl monomers are added to the methacrylic acid ester monomer, the composition ratio of the methacrylic acid ester monomer to the other vinyl monomer is The vinyl monomer is preferably 20 to 0% by mass with respect to 80 to 100% by mass of the acid ester monomer, and more preferably the composition ratio of methacrylic acid ester monomer / other vinyl monomers. Then, it is 90-100 mass% / 10-0 mass%, More preferably, it is 95-100 mass% / 5-0 mass%.
When it is particularly necessary to consider the polymerization stability, the blending amount of other vinyl monomers copolymerizable with the methacrylic acid ester monomer in the polymer (I) is substantially zero. In this case, the amount of the methacrylic acid ester monomer as a raw material is allowed to be present as an impurity.
When other vinyl monomer is added to the methacrylic acid ester monomer that is the raw material of the polymer (II), the composition ratio of the methacrylic acid ester monomer to the other vinyl monomer is methacrylic acid. The composition ratio of ester monomer / other vinyl monomer is preferably 80 to 99.5% by mass / 20 to 0.5% by mass, and 85 to 99.5% by mass / 15 to 0%. More preferably, the content is 0.5 mass%, more preferably 88 to 99 mass% / 12 to 1 mass%, and even more preferably 90 to 98.5 mass% / 10 to 1.5 mass%. preferable.

<Copolymerization ratio of vinyl monomer in polymer (I) and vinyl monomer in polymer (II)>
Each of the polymers (I) and (II) of the above-mentioned polymer (I) and polymer (II), “other vinyl monomer units copolymerizable with methacrylic acid esters” that can be used as a polymerization raw material. The copolymerization ratio in the inside is not particularly limited as long as the effect of the present invention can be exerted, but other vinyl monomer units copolymerizable with the methacrylic acid ester of the polymer (I) are not limited. When the composition ratio is Mal (mass%) and the composition ratio of other vinyl monomer units copolymerizable with the methacrylic acid ester of the polymer (II) is Mah (mass%), from the viewpoint of polymerization stability, It is preferable that the relationship of Formula (v) is established.
Mah ≧ Mal ≧ 0 (v)

The polymer (II) having a high molecular weight contains a larger amount of other vinyl monomers copolymerizable with methacrylic acid ester in the composition ratio, so that the polymerization stability can be improved and the heat resistance is improved. And fluidity can be improved while maintaining the mechanical strength.
More preferably, the relationship of the following formula (vi) is satisfied.
(Mah-0.8) ≧ Mal ≧ 0 (vi)

In the acrylic resin (methacrylic resin) obtained by the manufacturing method of the present embodiment, when a molded body is used, the flow rate is improved while reducing the occurrence rate of cracks and distortion of the molded body in the environmental test and maintaining the mechanical strength. When it is required to satisfy the following relationship, it is preferable to satisfy the relationship of the following formula (vii).
(Mah-2) ≧ Mal ≧ 0 (vii)

The composition ratio (Mal) of other vinyl monomer units copolymerizable with the methacrylic acid ester of the polymer (I) and other vinyl monomers copolymerizable with the methacrylic acid ester of the polymer (II). The amount of the composition ratio (Mah) of the unit is determined by measuring and determining the polymer (I) and the polymer (II) by pyrolysis gas chromatography.
In order to satisfy the above formulas, the respective composition ratios Mal and Mah are prepared by adjusting the amount of other vinyl monomers copolymerizable with the methacrylic acid ester monomer added during polymerization. do it.

(Manufacturing method of acrylic resin by suspension polymerization method)
In the acrylic resin production method, the case where the polymerization process is carried out by applying the suspension polymerization method will be described in detail.
When the acrylic resin is produced by suspension polymerization, the polymer (II) is polymerized in the presence of the polymer (I) in the above-described (first method) and (second method).
<Temperature and time>
When the acrylic resin is polymerized by suspension polymerization, the polymerization temperature is preferably 60 ° C. or higher and 90 ° C. or lower and 65 ° C. or higher and 85 ° C. or lower from the viewpoint of productivity and the amount of aggregates produced. Is more preferably 70 ° C. or more and 85 ° C. or less, and further preferably 70 ° C. or more and 83 ° C. or less.
The polymerization temperatures of the polymer (I) and the polymer (II) described above may be the same or different.
The time (T1) from the addition of the raw material mixture of the polymer (I) to the arrival of the exothermic peak temperature due to the polymerization exotherm is not particularly limited, but is preferably 20 minutes to 240 minutes, More preferably, it is 30 minutes or more and 210 minutes or less, more preferably 45 minutes or more and 180 minutes or less, even more preferably 60 minutes or more and 150 minutes or less, and even more preferably 60 minutes or more and 120 minutes or less. Even more preferred. The polymerization time (T1) may be appropriately adjusted by changing the amount of polymerization initiator used and the polymerization temperature.
The temperature at which the raw material mixture of the polymer (I) is added may be the same as or lower than the boiling point of the raw material to be used, considering the boiling point of the raw material to be used. Specifically, the temperature is preferably 60 ° C. or higher and 90 ° C. or lower, more preferably 60 ° C. or higher and 85 ° C. or lower, further preferably 65 ° C. or higher and 85 ° C. or lower, and 65 ° C. or higher and 80 ° C. or lower. More preferably, it is more preferably 70 ° C. or higher and 80 ° C. or lower.
The raw material mixture of the polymer (II) may be added immediately after an exothermic peak due to the polymerization of the polymer (I) is observed, or may be added after holding for a certain time. When it is necessary to increase the degree of polymerization of the raw material mixture of the polymer (I), after the exothermic peak due to the polymer (I) is confirmed, the raw material mixture of the polymer (II) is held for a certain period of time. Is preferably introduced.
The holding time is preferably 180 minutes or less, more preferably 10 minutes or more and 180 minutes or less, still more preferably 15 minutes or more and 150 minutes or less, still more preferably 20 minutes or more and 120 minutes or less, and even more preferably 20 minutes. It is 90 minutes or less.
Since the polymerization temperature can be increased, the temperature at the time of holding is preferably the same as the polymerization temperature of the polymer (I) or higher than the polymerization temperature of the polymer (I), and is set to a higher temperature. In this case, it is preferable to raise the temperature by 5 ° C. or more from the polymerization temperature. When the temperature is raised, the temperature is preferably 100 ° C. or lower from the viewpoint of preventing aggregation of the resulting polymer. Specifically, 80 ° C. or higher and 100 ° C. or lower is preferable, 80 ° C. or higher and 99 ° C. or lower is more preferable, 85 ° C. or higher and 99 ° C. or lower is further preferable, 88 ° C. or higher and 99 ° C. or lower is even more preferable, Is even more preferable.
By performing polymerization according to the polymerization temperature and polymerization time described above, polymer particles having a smaller angle of repose can be generated.
As described above, when the temperature is raised in the holding step, from the viewpoint of preventing volatilization of the raw material mixture of the polymer (II), the temperature is lowered to around 70 ° C. to 85 ° C., and then the raw material mixture of the polymer (II) is changed. It is preferable to add.
The time (T2) from when the raw material mixture of the polymer (II) is added until the exothermic peak temperature due to the polymerization exotherm is observed is not particularly limited, but is preferably 30 minutes or more and 240 minutes or less. More preferably, they are 45 minutes or more and 210 minutes or less, More preferably, they are 60 minutes or more and 210 minutes or less, More preferably, they are 60 minutes or more and 180 minutes or less, More preferably, they are 80 minutes or more and 150 minutes or less.

The relationship between the polymerization times of the polymer (I) and the polymer (II) is such that the polymer (I) can be obtained from the viewpoint that productivity and an acrylic resin having a small difference in weight average molecular weight for each particle diameter can be obtained. Polymerization time, that is, the time (T1) until the exothermic peak temperature is reached due to polymerization exotherm after addition of the monomer in the first stage polymerization, and the polymerization time of the polymer (II), that is, a single amount after the second stage. It is preferable that the following formula (3) holds for the time (T2) to reach the exothermic peak temperature due to polymerization exotherm after adding the body.
T2 / T1 ≧ 1 (3)
In particular, when it is necessary to obtain polymer particles having a uniform molecular weight distribution, and further, it is necessary to suppress the formation of aggregates that contribute to a decrease in yield, 1 ≦ T2 / T1 ≦ 5 may be satisfied. More preferably, 1 ≦ T2 / T1 ≦ 4, and further preferably 1 ≦ T2 / T1 ≦ 3.

In order to adjust the time required to reach the first and second exothermic peak temperatures so as to satisfy the above formula (3), the polymerization ratio of the polymer (I) and the polymer (II) is adjusted. The polymerization temperature may be adjusted, or the amount of the polymerization initiator to be used may be appropriately adjusted.
After the exothermic peak temperature due to the polymerization exotherm is observed after the addition of the polymer (II) raw material mixture, the amount of residual monomer in the resulting acrylic resin (methacrylic resin) can be suppressed. It is preferable to raise the temperature by 5 ° C. or more than the polymerization temperature of (II).
More preferably, the temperature is raised to 7 ° C or higher, more preferably 10 ° C or higher.
Moreover, in order to prevent aggregation of the obtained resin, it is preferable that the reached temperature is 100 ° C. or lower, and a preferable temperature range is 85 ° C. or higher and 100 ° C. or lower, more preferably 88 ° C. or higher and 99 ° C. or lower. Preferably they are 90 degreeC or more and 99 degrees C or less.
The time for maintaining the temperature after the temperature rise is preferably 15 minutes or more and 360 minutes or less, more preferably 30 minutes or more and 240 minutes or less, and more preferably 30 minutes or more and 180 minutes in consideration of the residual monomer reduction effect. More preferably, it is 30 minutes or more and 150 minutes or less, and more preferably 30 minutes or more and 120 minutes or less.

<Washing method>
The obtained polymer slurry is preferably subjected to operations such as acid washing, water washing and alkali washing for removing the suspending agent, and the number of times these washing operations are carried out depends on work efficiency and suspending agent removal efficiency. What is necessary is just to choose the optimal number, and it may be repeated once or several times.
What is necessary is just to select the temperature at the time of washing | cleaning in consideration of the removal efficiency of a suspension agent, the coloring degree of the polymer obtained, etc., and it is preferable that it is 20-100 degreeC. More preferably, it is 30-95 degreeC, More preferably, it is 40-95 degreeC.
Moreover, it is preferable that the washing | cleaning time per time at the time of washing | cleaning is 10 to 180 minutes from a viewpoint of washing | cleaning efficiency, a repose angle reduction effect, and the simplicity of a process, More preferably, it is 20 to 150 minutes.
The pH of the cleaning solution used at the time of the cleaning may be within a range where the suspension can be removed, but is preferably pH 1-12. The pH for acid washing is preferably pH 1-5, more preferably pH 1.2-4, from the viewpoint of the removal efficiency of the suspending agent and the color tone of the resulting polymer.
The acid used at that time is not particularly limited as long as it can remove the suspending agent. Conventionally known inorganic acids and organic acids can be used. As an example of the acid that is preferably used, the inorganic acid includes hydrochloric acid, nitric acid, sulfuric acid, phosphoric acid, boric acid and the like, and each may be used in a diluted solution diluted with water or the like. Examples of the organic acid include those having a carboxyl group, a sulfo group, a hydroxy group, a thiol group, or an enol. Considering the effect of removing the suspending agent and the color tone of the resulting resin, more preferred are nitric acid, sulfuric acid, and organic acids having a carboxyl group.
After the acid cleaning, it is preferable to further perform water washing or alkali washing from the viewpoint of reducing the color tone and angle of repose of the polymer obtained.
The pH of the alkaline solution when performing alkali cleaning is preferably pH 7.1 to 12, more preferably 7.5 to 11, and still more preferably 7.5 to 10.5.
As the alkaline component used for alkali cleaning, tetraalkylammonium hydroxide, alkali metal hydroxide, alkaline earth metal hydroxide, and the like are preferably used. More preferred are alkali metal hydroxides and alkaline earth metal hydroxides, and further preferred are lithium hydroxide, sodium hydroxide, potassium hydroxide, rubidium hydroxide, cesium hydroxide, magnesium hydroxide, calcium hydroxide, Barium hydroxide is more preferable, and lithium hydroxide, sodium hydroxide, potassium hydroxide, magnesium hydroxide, and calcium hydroxide are more preferable, and sodium hydroxide and potassium hydroxide are still more preferable. These alkaline components can be used by adjusting the pH by diluting with water or the like.

<Dehydration process>
As a method for separating the polymer particles from the obtained polymer slurry, a conventionally known method can be applied.
For example, a dehydration method using a centrifuge that shakes off water using centrifugal force, a method of sucking and removing water on a perforated belt or a filtration membrane, and the like can be mentioned.

<Drying process>
The polymer in a water-containing state obtained through the dehydration step can be recovered after being dried by a known method.
For example, hot air drying for drying by sending hot air into the tank from a hot air blower or blow heater, etc., vacuum drying for drying by heating as necessary after reducing the pressure inside the system, and obtained polymer For example, barrel drying for removing moisture by rotating the container in a container, spin drying for drying using centrifugal force, and the like. These methods may be used alone or in combination.
The water content of the obtained resin is preferably 0.1% by mass to 1% by mass, more preferably 0.15% by mass to 1% by mass, from the viewpoints of handleability, color tone, and the like. More preferably, the content is 2% by mass to 1% by mass, and even more preferably 0.27% by mass to 1% by mass.
The water content of the resin can be measured using the Karl Fischer method.

<Aggregates>
When an acrylic resin is produced using a suspension polymerization method, the resulting acrylic resin is substantially spherical, but an aggregate may be formed in part.
The said aggregate refers to the residue which remains on a sieve, when the obtained polymer is passed through a 1.68 mm mesh sieve.
When the aggregate remains in the acrylic resin, the color tone of the acrylic resin tends to decrease.
The amount of the aggregate in the acrylic resin is preferably 1.2% by mass or less, and more preferably 1.0% by mass or less.
The agglomerate content was passed through a 1.68 mm mesh sieve, and the weight of what was left on the sieve was dried in a drying oven at 80 ° C. for 12 hours, and the obtained weight was the total amount of raw materials. The amount of industry type generated (mass%) can be calculated.

[Composition of acrylic resin]
The acrylic resin of the present embodiment can be used as a composition in combination with a predetermined other resin and a predetermined additive described later.
<Other resins>
The resin to be combined is not particularly limited, and known curable resins and thermoplastic resins are preferably used.
For example, thermoplastic resins include polypropylene resin, polyethylene resin, polystyrene resin, syndiotactic polystyrene resin, ABS resin, acrylic resin, AS resin, BAAS resin, MBS resin, AAS resin, raw resin Decomposable resin, polycarbonate-ABS resin alloy, polybutylene terephthalate, polyethylene terephthalate, polypropylene terephthalate, polytrimethylene terephthalate, polyethylene naphthalate and other polyalkylene arylate resins, polyamide resins, polyphenylene ether resins, polyphenylene sulfide resins And phenolic resins.
In particular, AS resin and BAAS resin are preferable because the effect of improving the fluidity of the resin composition is obtained, ABS resin and MBS resin are preferable for improving impact resistance, and polyester resin has chemical resistance. It is preferable for improvement. In addition, polyphenylene ether resins, polyphenylene sulfide resins, phenol resins, and the like can be expected to have an effect of improving flame retardancy.
Examples of the curable resin include unsaturated polyester resin, vinyl ester resin, diallyl phthalate resin, epoxy resin, cyanate resin, xylene resin, triazine resin, urea resin, melamine resin, benzoguanamine resin, urethane resin, oxetane resin, Examples include ketone resins, alkyd resins, furan resins, styrylpyridine resins, silicone resins, and synthetic rubbers.
These resins may be used alone or in combination of two or more resins.

<Additives>
A predetermined additive may be added to the acrylic resin of this embodiment in order to impart various characteristics such as rigidity and dimensional stability.
Additives include, for example, various stabilizers such as antioxidants, ultraviolet absorbers, heat stabilizers, light stabilizers; plasticizers (paraffinic process oil, naphthenic process oil, aromatic process oil, paraffin, organic Polysiloxane, mineral oil), flame retardants (eg, phosphorus compounds such as organic phosphorus compounds, red phosphorus, inorganic phosphates, halogens, silicas, silicones, etc.), flame retardant aids (eg, antimony oxides) , Metal oxides, metal hydroxides, etc.), curing agents (diethylenetriamine, triethylenetetramine, tetraethylenepentamine, pentaethylenehexamine, diethylaminopropylamine, 3,9-bis (3-aminopropyl) -2,4, 8,10-tetraoxaspiro [5,5] undecane, mensendiamine, isophoronediamine, N-amino Amines such as ethylpiperazine, m-xylenediamine, m-phenylenediamine, diaminophenylmethane, diaminodiphenylsulfone, dicyandiamide, adipic dihydrazide, phenolic resins such as phenol novolac resin and cresol novolac resin, liquid polymercaptan, Polymercaptan such as polysulfide, maleic anhydride, phthalic anhydride, tetrahydrophthalic anhydride, hexahydrophthalic anhydride, methyltetrahydrophthalic anhydride, methylhexahydrophthalic anhydride, methyl nadic anhydride, pyromellitic anhydride, methylcyclohexenetetra Carboxylic anhydride, dodecyl succinic anhydride, trimellitic anhydride, chlorendic anhydride, benzophenone tetracarboxylic anhydride, ethylene glycol bis ( Acid anhydrides such as anhydrotrimate), curing accelerators (2-methylimidazole, 2-ethylimidazole, 2-ethyl-4-methylimidazole, 2-phenylimidazole, 2-undecylimidazole, 2-hepta) Imidazoles such as decylimidazole and 2-phenyl-4-methylimidazole, organic phosphines such as triphenylphosphine and tributylphosphine, benzyldimethylamine, 2-dimethylaminomethyl) phenol, 2,4,6-tris (diaminomethyl) ) Tertiary amines such as phenol and tetramethylhexanediamine, boron salts such as triphenylphosphine tetraphenylborate, tetraphenylphosphonium tetraphenylborate and triethylaminetetraphenylborate, 1,4-benzoquino 1,4-naphthoquinone, 2,3-dimethyl-1,4-benzoquinone, 2,6-dimethylbenzoquinone, quinoid compounds such as 2,3-dimethoxy-1,4-benzoquinone, etc.), antistatic agents (for example, Polyamide elastomer, quaternary ammonium salt system, pyridine derivative, aliphatic sulfonate, aromatic sulfonate, aromatic sulfonate copolymer, sulfate ester salt, polyhydric alcohol partial ester, alkyldiethanolamine, alkyldiethanolamide, Polyalkylene glycol derivatives, betaines, imidazoline derivatives, etc.), conductivity imparting agents, stress relieving agents, mold release agents (alcohols, esters of alcohols and fatty acids, esters of alcohols and dicarboxylic acids, silicone oils, etc.), crystals Accelerator, hydrolysis inhibitor, lubricant (e.g., Higher fatty acids such as theatric acid, behenic acid, zinc stearate, calcium stearate, magnesium stearate, and the like, and higher fatty acid amides such as ethylene bisstearamide), impact imparting agents, slidability improvers ( Hydrocarbons such as low molecular weight polyethylene, higher alcohols, polyhydric alcohols, polyglycols, polyglycerols, higher fatty acids, higher fatty acid metal salts, fatty acid amides, esters of fatty acids and fatty alcohols, full of fatty acids and polyhydric alcohols Esters or partial esters, full or partial esters of fatty acids and polyglycols, silicones, fluororesins, etc., compatibilizers, nucleating agents, reinforcing agents, flow control agents, dyes (nitroso dyes, nitro dyes, azo dyes) , Stilbene azo dye, ketoimine dye, triphenylmethane dye , Xanthene dye, acridine dye, quinoline dye, methine / polymethine dye, thiazole dye, indamine / indophenol dye, azine dye, oxazine dye, thiazine dye, sulfur dye, aminoketone / oxyketone dye, anthraquinone dye, indigoid dye, phthalocyanine dye, etc. Dyes), sensitizers, colorants (titanium oxide, carbon black, titanium yellow, iron oxide pigments, ultramarine, cobalt blue, chromium oxide, spinel green, lead chromate pigments, inorganic pigments such as cadmium pigments, Azo lake pigments, benzimidazolone pigments, diarylide pigments, azo pigments such as condensed azo pigments, phthalocyanine pigments such as phthalicyanine blue and phthalocyanine green, isoindolinone pigments, quinophthalone pigments, quinacridone pigments, peri Pigments, anthraquinone pigments, perinone pigments, organic pigments such as condensed polycyclic pigments such as dioxazine violet, scaly aluminum metallic pigments, spherical aluminum pigments used to improve weld appearance, Mica powder for pearl-like metallic pigments, other metallic pigments such as those coated by metal plating or sputtering on polyhedral particles of inorganic materials such as glass), rubbery polymers, thickeners, anti-settling agents, anti-sagging agents, Fillers (glass fibers, fibrous reinforcing agents such as carbon fibers, glass beads, calcium carbonate, talc, clay, etc.), antifoaming agents (silicone antifoaming agents, surfactants, polyethers, higher alcohols, etc.) Organic defoaming agents, etc.), coupling agents, rust inhibitors, antibacterial / antifungal agents, antifouling agents, conductive polymers and the like.
Examples of the heat stabilizer include participation inhibitors such as hindered phenol antioxidants and phosphorus processing stabilizers, and hindered phenol antioxidants are preferable. Specifically, pentaerythritol tetrakis [3- (3,5-di-tert-butyl-4-hydroxyphenyl) propionate], thiodiethylenebis [3- (3,5-di-tert-butyl-4-hydroxy) Phenyl) propionate], octadecyl-3- (3,5-di-tert-butyl-4-hydroxyphenyl) propionate, 3,3 ′, 3 ″, 5,5 ′, 5 ″ -hexa-tert-butyl -A, a ', a''-(mesitylene-2,4,6-triyl) tri-p-cresol, 4,6-bis (octylthiomethyl) -o-cresol, 4,6-bis (dodecylthio) Methyl) -o-cresol, ethylenebis (oxyethylene) bis [3- (5-tert-butyl-4-hydroxy-m-tolyl) propionate], hexamethylenebis [3- (3,5-di-tert- Butyl-4 -Hydroxyphenyl) propionate], 1,3,5-tris (3,5-di-tert-butyl-4-hydroxybenzyl) -1,3,5-triazine-2,4,6 (1H, 3H, 5H ) -Trione, 1,3,5-tris [(4-tert-butyl-3-hydroxy-2,6-xylin) methyl] -1,3,5-triazine-2,4,6 (1H, 3H, 5H) -trione, 2,6-di-tert-butyl-4- (4,6-bis (octylthio) -1,3,5-triazin-2-ylamine) phenol, and the like. In particular, pentaerythritol terakis [3- (3,5-di-tert-butyl-4-hydroxyphenyl) propionate] is preferable.
Examples of the ultraviolet absorber include benzotriazole compounds, benzotriazine compounds, benzoate compounds, benzophenone compounds, oxybenzophenone compounds, phenol compounds, oxazole compounds, malonic ester compounds, cyanoacrylate compounds, Examples include lactone compounds, salicylic acid ester compounds, benzoxazinone compounds, and the like. In particular, benzotriazole compounds and benzotriazine compounds are preferable. These may be used alone or in combination of two or more.
The ultraviolet absorber preferably has a vapor pressure (P) at 20 ° C. of 1.0 × 10 ⁻⁴ Pa or less from the viewpoint of ensuring good molding or configuration of the thermoplastic resin obtained in the present embodiment. It is more preferably 1.0 × 10 ⁻⁶ Pa or less, and further preferably 1.0 × 10 ⁻⁸ Pa or less.
Here, good moldability means that, for example, when a film is molded, there is little adhesion of a low molecular compound to a roll. When it adheres to the roll, it reattaches to the surface, which causes the appearance to deteriorate and the optical characteristics to deteriorate.
The melting point (Tm) of the ultraviolet absorber is preferably 80 ° C. or higher, more preferably 100 ° C. or higher, further preferably 130 ° C. or higher, and even more preferably 160 ° C. or higher. preferable.
The ultraviolet absorber preferably has a weight reduction rate of 50% or less, more preferably 30% or less, and more preferably 15% or less when the temperature is increased from 23 ° C. to 260 ° C. at a rate of 20 ° C./min. More preferably, it is more preferably 10% or less, still more preferably 5% or less.

<Additives and other resin kneading methods>
A conventionally known method can be used as a kneading method when the acrylic resin of this embodiment is processed or mixed with various additives or other resins, and is not particularly defined.
For example, it can knead | mix using kneading machines, such as an extruder, a heating roll, a kneader, a roller mixer, a Banbury mixer.
Among these, kneading with an extruder is preferable in terms of productivity.
The kneading temperature may be in accordance with the preferred processing temperature of the resin or other resin to be mixed, and is generally in the range of 140 to 300 ° C, preferably in the range of 180 to 280 ° C.

[Molded body]
It can be set as a molded object by shape | molding the acrylic resin of this embodiment independently or the resin composition containing this.
As a method for producing a molded body, known methods such as injection molding, sheet molding, blow molding, injection blow molding, inflation molding, T-die molding, press molding, extrusion molding, foam molding, film molding by casting method, and the like are applied. Secondary processing molding methods such as pressure forming and vacuum forming can also be used.
Moreover, when using the resin composition which mix | blended curable resin with the acrylic resin of this embodiment, the component for manufacturing a resin composition can be mixed uniformly without a solvent or as needed. After mixing with a solvent, the solvent is removed to obtain a resin composition, which is cast into a mold, cured, cooled, and taken out of the mold to obtain a molded product.
It can also be cast into a mold and cured by hot pressing. The solvent for dissolving each component is not particularly limited as long as various materials can be uniformly mixed and the properties of the acrylic resin of the present embodiment are not impaired by use. Absent. For example, toluene, xylene, acetone, methyl ethyl ketone, methyl butyl ketone, diethyl ketone, cyclopentanone, cyclohexanone, dimethylformamide, methyl cellosolve, methanol, ethanol, n-propanol, iso-propanol, n-butanol, n-pentanol , N-hexanol, cyclohexanol, n-hexane, n-pentane and the like.
Another example is a method in which a resin composition is kneaded and produced using a kneader such as a heating roll, kneader, Banbury mixer, extruder, etc., then cooled, pulverized, and further molded by transfer molding, injection molding, compression molding or the like Can be mentioned. The curing method varies depending on the curing agent used, but is not particularly limited. Examples include thermal curing, light curing, UV curing, pressure curing, moisture curing, and the like. The order of mixing the components is not particularly limited as long as the effect of the present invention can be achieved.

[Use]
The acrylic resin of this embodiment and the resin composition using the same can be suitably used as materials for various molded products.
Examples of the usage of the molded body include household items, OA equipment, AV equipment, battery electrical equipment, lighting equipment, automobile parts use, housing use, sanitary use, ball game machine use, liquid crystal display, plasma display, and organic EL. Light guide plate, diffuser plate, polarizing plate protective film, quarter wave plate, half wave plate, viewing angle control film, liquid crystal optical compensation film, etc. used in displays such as displays, field emission displays, rear projection televisions, etc. Examples thereof include a phase difference film, a display front plate, a display substrate, a lens, and a touch panel, and can be suitably used for a transparent substrate used for a solar cell. In addition, in the fields of optical communication systems, optical switching systems, and optical measurement systems, they can also be used for waveguides, lenses, optical fibers, optical fiber coating materials, LED lenses, lens covers, and the like. It can also be used as a modifier for other resins.
The molded body using the acrylic resin and the resin composition of the present embodiment may be subjected to surface functionalization treatment such as antireflection treatment, transparent conductive treatment, electromagnetic wave shielding treatment, and gas barrier treatment.

  EXAMPLES Hereinafter, although an Example demonstrates this invention concretely, this invention is not limited to the following examples.

〔material〕
The raw materials used are as follows.
・ Methyl methacrylate (MMA): Made by Asahi Kasei Chemicals (2.5 ppm of 2,4-di-6-tert-butylphenol) was added as a polymerization inhibitor. What is being done)
・ Methyl acrylate (MA): manufactured by Mitsubishi Chemical (added with 14 ppm of 4-methoxyphenol manufactured by Kawaguchi Chemical Industry as a polymerization inhibitor)
-N-octylmercaptan (N-octylmercaptan): manufactured by Arkema-2-ethylhexyl thioglycolate: manufactured by Arkema-Lauroyl peroxide: manufactured by Nippon Oil & Fats-Calcium phosphate: Made by Nippon Kagaku Kogyo Co., Ltd., used as a suspension agent. Calcium carbonate: Made by Shiraishi Kogyo Co., Ltd., used as a suspension agent. Sodium lauryl sulfate, made by Wako Pure Chemical Industries, Ltd., used as a suspension aid.

〔Measuring method〕
(I. Measurement of resin composition and molecular weight)
<1. Composition analysis of acrylic resin>
The composition analysis of the acrylic resin was performed by pyrolysis gas chromatography and mass spectrometry.
Pyrolysis device: PY-2020D made by FRONTIER LAB
Column: DB-1 (length 30 m, inner diameter 0.25 mm, liquid phase thickness 0.25 μm)
Column temperature program: held at 40 ° C. for 5 min, then raised to 320 ° C. at a rate of 50 ° C./min, held at 320 ° C. for 4.4 minutes Pyrolysis furnace temperature: 550 ° C.
Column inlet temperature: 320 ° C
Gas chromatography: Agilent GC6890
Carrier: pure nitrogen, flow rate 1.0 mL / min
Injection method: Split method (split ratio 1/200)
Detector: JEOL mass spectrometer Automass Sun
Detection method: Electron impact ionization method (ion source temperature: 240 ° C., interface temperature: 320 ° C.)
Sample: 10 μL of 10 g chloroform solution of 0.1 g acrylic resin

A sample was collected in a platinum sample cup for a thermal decomposition apparatus, vacuum-dried at 150 ° C. for 2 hours, and then the sample cup was placed in a thermal decomposition furnace, and composition analysis of the sample was performed under the above conditions.
Based on the peak area on the total ion chromatography (TIC) of methyl methacrylate and methyl acrylate and the calibration curve of the following standard sample, the composition ratio of the acrylic resin was determined.

Preparation of standard sample for calibration curve: The ratio of methyl methacrylate and methyl acrylate is (methyl methacrylate / methyl acrylate) = (100 mass% / 0 mass%), (98 mass% / 2 mass%), (94 (Mass% / 6 mass%), (90 mass% / 10 mass%), (80 mass% / 20 mass%), a total of 5 kinds of solutions, 50 g of each, lauroyl peroxide 0.25 mass%, n-octyl Mercaptan (0.25% by mass) was added.
Each mixed solution was put into a 100 cc glass ampule bottle, and the air was replaced with nitrogen and sealed.
The glass ampoule bottle was placed in an 80 ° C. water bath for 3 hours and then in an oven at 150 ° C. for 2 hours.
After cooling to room temperature, the glass was crushed, the acrylic resin inside was taken out, and composition analysis was performed.
A graph of (methyl acrylate area value) / (methyl methacrylate area value + methyl acrylate area value) and methyl acrylate charge ratio obtained by measurement of a standard sample for a calibration curve is used as a calibration curve. It was.

<2. Measurement of weight average molecular weight (Mw) and molecular weight distribution of acrylic resin>
Measuring apparatus: Nippon Analytical Industry Gel Permeation Chromatography (LC-908)
Column: 1 JAIGEL-4H and 2 JAIGEL-2H in series connection In this column, the high molecular weight elutes early, and the low molecular weight elutes slowly.
Detector: RI (differential refraction) detector Detection sensitivity: 2.4 μV / sec
Sample: 0.450 g acrylic resin in chloroform (15 mL) Injection volume: 3 mL
Developing solvent: chloroform, flow rate 3.3 mL / min

Under the above conditions, the RI detection intensity with respect to the elution time of the acrylic resin was measured.
Based on the area area in the GPC elution curve and the calibration curve, the weight average molecular weight (Mw) and molecular weight distribution (Mw / Mn) of the acrylic resin were determined.
The following 10 methacrylic resins (manufactured by EasiCal PM-1 Polymer Laboratories) having different molecular weights and known monodispersed weight average molecular weights were used as standard samples for calibration curves.

Weight average molecular weight (Mw)
Standard sample 1 1,900,000
Standard sample 2 790,000
Standard sample 3 281,700
Standard sample 4 144,000
Standard sample 5 59,800
Standard sample 6 28,900
Standard sample 7 13,300
Standard sample 8 5,720
Standard sample 9 1,936
Standard sample 10 1,020

  When the polymer (I) having a weight average molecular weight of 5,000 to 50,000 and the polymer (II) having a weight average molecular weight of 60,000 to 350,000 are mixed, the polymer (I) alone The GPC elution curve is measured to determine the weight average molecular weight, and the ratio of the polymer (I) present (in this specification, the charge ratio is used) is used as the GPC elution curve of the polymer (I). Multiplying and subtracting the detected intensity at the elution time from the GPC elution curve in which the polymer (I) and the polymer (II) are mixed together yields the GPC elution curve of the polymer (II) alone. From this, the weight average molecular weight of the polymer (II) was determined.

Further, the peak molecular weight (Mp) in the GPC elution curve was determined from the GPC elution curve and the calibration curve, and the molecular weight component of 1/5 or less of the Mp was determined as follows.
First, the area area (shaded area in FIG. 2) in the GPC elution curve of the acrylic resin is obtained. Next, the area area in the GPC elution curve is divided by the elution time corresponding to the molecular weight of 1/5 of Mp, and the area area in the GPC elution curve corresponding to the molecular weight component of 1/5 or less of Mp is obtained. From the ratio of the area to the area of the GPC elution curve, the ratio of molecular weight components equal to or less than 1/5 of Mp was determined. The measurement results are shown in Table 4 below.

<3. Measurement of composition ratio of vinyl monomer copolymerizable with methyl methacrylate in high molecular weight component and low molecular weight component of acrylic resin>
A high molecular weight component having a cumulative area area of 0 to 2% and a low molecular weight component having a cumulative area area of 98 to 100% shown in FIG. Went. Regarding the fractionation and measurement of components, the above-mentioned <1. Analysis of composition of acrylic resin> The same apparatus and conditions as in the above were used.
The fractionation was performed twice, and 10 μL of the fractionated sample was subjected to the above <1. Composition analysis of acrylic resin> The sample was collected in a platinum sample cup for a thermal decomposition apparatus used in pyrolysis gas chromatography analysis and mass spectrometry, and dried for 40 minutes with a vacuum dryer at 100 ° C. <1. Composition Analysis of Acrylic Resin> The composition of the acrylic resin corresponding to the accumulated area area fractionated under the same conditions as those described above was determined.
Vinyl monomer copolymerizable with methyl methacrylate in high molecular weight component (molecular weight component in cumulative area area 0-2%; Mh) and low molecular weight component (molecular weight component in cumulative area area 98-100%; Ml) Table 4 shows the measurement results of the composition ratio of (MA: methyl acrylate).

(II. Measurement of aggregate production)
The mixed solution containing polymer fine particles obtained by polymerization is passed through a 1.68 mm mesh sieve to remove fine particle aggregates, and the obtained aggregates are dried in a drying oven at 80 ° C. for 12 hours. It was measured.
The obtained weight is the total amount of the raw material (I) for synthesizing the polymer (I) and the raw material (II) for synthesizing the polymer (II) (acrylic resins of Examples and Comparative Examples described later) Divided by the total amount of raw materials), and the aggregate production amount (% by mass) was calculated. Shown in Table 3 below.

(III. Difference in fine particle sieving, average particle diameter, weight average molecular weight)
Based on JIS-Z8801, sieve <Tokyo Screen JTS-200-45-33 (aperture 500 μm), 34 (aperture 425 μm), 35 (aperture 355 μm), 36 (aperture 300 μm), 37 (aperture 250 μm) ), 38 (aperture 150 μm), 61 (dish)>, and the weight of particles remaining on each sieve when sieving with vibrational force MAX for 10 minutes using a sieve tester TSK B-1 was measured. And the average particle diameter was calculated | required by calculating | requiring the particle diameter when a weight will be 50%. The average particle size is shown in Table 4 below.
At this time, the weight average molecular weight (A) of particles remaining at an opening of 500 μm (particles having a particle diameter of 500 μm or more) and the weight average molecular weight of particles remaining at an opening of 300 μm (particles having a particle diameter of 355 μm to 300 μm) (B ), The weight average molecular weight (C) of the particles of the saucer (particles having a particle diameter of 150 μm or less) was measured by gel permeation chromatography, and the difference in the weight average molecular weight was absolutely expressed by the following formulas (1) and (2). Calculated by value.
| [(A)-(B)] / (B) | × 100 (%) (1)
| [(C)-(B)] / (B) | × 100 (%) (2)
The calculated values of the formulas (1) and (2) are shown in Table 3 below.

(IV. Physical property measurement)
<1. Measurement of spiral length>
This is a test for determining the relative fluidity based on the distance of the resin flowing through a spiral cavity having a constant cross-sectional area.
Injection molding machine: Toshiba Machine IS-100EN
Mold for measurement: Mold having a groove with a depth of 2 mm and a width of 12.7 mm dug in the Archimedes spiral shape from the center of the surface on the mold surface Injection conditions Resin temperature: 250 ° C.
Mold temperature: 55 ° C
Injection pressure: 98 MPa
Injection time: 20 sec
Resin was injected into the center of the mold surface under the above conditions. After 40 seconds from the end of injection, the spiral shaped product was taken out and the length of the spiral portion was measured. The measured values of the spiral length are shown in Table 5 below. This was used as an index for liquidity evaluation.
When the spiral part was long, it was judged that the fluidity was good.

<2. Break time measurement by cantilever method>
The solvent resistance was evaluated by the measuring method by the cantilever method shown in FIG.
Injection molding machine: Toshiba Machine IS-100EN
Injection molded body: thickness 3.2 mm, width 12.7 mm, length 127 mm
Injection conditions Molding temperature: 230 ° C
Mold temperature: 60 ℃
Injection pressure: 56MPa
Injection time: 20 sec
Cooling time: 40 sec
The molded body molded under the above conditions was stored in a desiccator for 1 day so as not to absorb water.
Thereafter, using the jig 1 shown in FIG. 1, the molded body 2 is installed as shown in FIG. 1, and a 3 kg weight 3 with an octopus thread 5 attached thereto is attached as shown in FIG. 1, and a filter paper 4 containing ethanol. Was placed at the position shown in FIG. 1, and the time until the molded body was broken by the weight 3 was measured from the placed time.
Repeated 10 times for each sample, the maximum time and minimum time data were deleted, and the average of the remaining 8 times was determined. This was used as an index for solvent resistance evaluation. Table 5 below shows the time to break (break time).

<3. Measurement of VICAT softening temperature>
In accordance with ISO 306 B50, measurement was performed using a 4 mm-thick test piece to obtain a VICAT softening temperature, which was used as an index for heat resistance evaluation. The measured values of the VICAT softening temperature are shown in Tables 3 and 5 below.

<4. Transparency>
Based on the ISO 13468-1 standard, the total light transmittance was measured using a 3 mm-thick test piece, and used as an index of transparency. The measured values of total light transmittance are shown in Table 5 below.

<5. Deflection temperature under load>
Measurements were performed in accordance with ISO 75-2 / A standard and used as an index for heat resistance evaluation.

<6. Tensile test>
In accordance with the ISO 527-2 standard, tensile modulus, tensile yield stress, and tensile fracture strain were measured using a 1A type dumbbell test piece.

<7. Charpy impact strength (no notch)>
Measurement was performed in accordance with the ISO 179 / 1eU standard and used as an index of impact resistance.

<8. Evaluation of color tone>
Using a color difference meter “TC-8600A” manufactured by Nippon Denshoku Industries Co., Ltd., four test pieces having a thickness of 3 mm × 20 mm × a length of 220 mm were used, and JIS T7105 (plastic optical property test method) , YI (yellowness) in the length direction of 220 mm was measured, and yellowness ΔYI was measured using the following equation.
ΔYI indicates the degree of yellowing of the molded product, and the smaller the value, the smaller the coloring.
Yellowness difference ΔYI = YI−YI0
ΔYI = Yellowness difference YI = Yellowness of molded body YI0 = Yellowness of air The obtained ΔYI value is less than 20, “◯”, 20 to less than 30 “Δ”, and 30 or more “×” Was evaluated in three stages.
The evaluation results are shown in Table 3 below.

[Example 1]
2 kg of water, 65 g of tribasic calcium phosphate, 39 g of calcium carbonate, and 0.39 g of sodium lauryl sulfate were charged into a container having a stirrer to obtain a mixed solution (A).
Next, 26 kg of water was charged into a 60 L reactor and the temperature was raised to 80 ° C., and the mixture (A) and the raw material (I) for producing the polymer (I) with the blending amounts shown in Table 1 below were used. ).
Thereafter, suspension polymerization was performed while maintaining the temperature at about 80 ° C., and an exothermic peak was observed 80 minutes after the starting material of the polymer (I) was added.
Thereafter, the temperature was raised to about 92 ° C. at a rate of 1 ° C./min, and then maintained at a temperature of 92 ° C. to 94 ° C. for 30 minutes.
Thereafter, the temperature was lowered to 80 ° C. at a rate of 1 ° C./min, and then the raw material (II) for producing the polymer (II) was added to the reactor in the blending amount shown in Table 1 below, followed by about 80 ° C. The suspension polymerization was carried out while maintaining the temperature, and an exothermic peak was observed 130 minutes after charging the raw material of the polymer (II).
Thereafter, the temperature was raised to about 92 ° C. at a rate of 1 ° C./min and then aged for 60 minutes to substantially complete the polymerization reaction.
Next, in order to cool to 50 ° C. and dissolve the suspending agent, 20 mass% sulfuric acid was added.
Next, the polymerization reaction solution was passed through a 1.68 mm mesh sieve to remove aggregates, and the resulting bead polymer was washed and dehydrated to obtain polymer fine particles.
It was 0.23 mass% when the aggregate production amount (mass%) was measured by the method described in said (II. Measurement of aggregate production amount).
The obtained polymer fine particles were dried in a drying oven at 80 ° C. for 12 hours, followed by sieving the polymer fine particles and measuring the difference in weight average molecular weight. In the measurement), the calculated value by the formula (1) was 0.9%, and the calculated value by the formula (2) was 1.6%.

The obtained polymer fine particles were melt-kneaded using a φ30 mm twin screw extruder set at 240 ° C., and the strands were cooled and cut to obtain resin pellets. At that time, the extrusion workability was good.
The obtained pellets had a weight average molecular weight (Mw) of 118,000 and a molecular weight distribution (Mw / Mn) of 3.3.
Moreover, when the fluidity | liquidity of the obtained resin pellet was measured by MFR, it was 1.7 g / 10min.
When the tensile properties were measured, the tensile modulus was 3300 MPa, the tensile yield stress was 75 MPa, and the tensile fracture strain was 6%.
Furthermore, when Charpy impact strength (without notch) was measured as an index of impact resistance, it was 22 kJ / m ² . Moreover, when the VICAT softening temperature was measured, it was 109 degreeC and the deflection temperature under load was 100 degreeC.

[Examples 2 to 11], [Comparative Examples 1 to 4]
Polymerization was performed using the raw materials shown in Table 1 in the same manner as in Example 1 to obtain polymer fine particles.
Table 2 shows the monomer charge composition of polymer (I) and polymer (II) and the ratio of polymers (I) and (II).
Time (T1) from when the raw material of the polymer (I) is introduced until the exothermic peak is reached, time (T2) from when the raw material of the polymer (II) is introduced until the exothermic peak is reached, and aggregate production amount The measurement results (mass%) and the difference in molecular weight (calculated values of formula (1) and formula (2)) are shown in Table 3 below.
Further, resin pellets were produced in the same manner as in Example 1. The results of measuring the weight average molecular weight (Mw) are shown in Table 3. In Comparative Examples 1 to 4, the strands were not stable during the extrusion operation, and the strands were sometimes broken.

Example 12
Into a container having a stirrer, 2 kg of water, 65 g of tricalcium phosphate, 39 g of calcium carbonate, and 0.39 g of sodium lauryl sulfate were added to obtain a mixed solution (A).
Next, 26 kg of water was charged into a 60 L reactor and the temperature was raised to 80 ° C., and the mixture (A) and the raw material (I) for producing the polymer (I) with the blending amounts shown in Table 1 below were used. ).
Thereafter, suspension polymerization was performed while maintaining the temperature at about 80 ° C., and an exothermic peak was observed 65 minutes after the starting material of the polymer (I) was added.
Thereafter, after maintaining the temperature at 80 ° C. for 30 minutes, the raw material (II) for producing the polymer (II) was charged into the reactor at the blending amount shown in Table 1 below, and kept at about 80 ° C. Suspension polymerization was carried out, and an exothermic peak was observed 130 minutes after charging the raw material of the polymer (II).
Thereafter, the temperature was raised to about 92 ° C. at a rate of 1 ° C./min and then aged for 60 minutes to substantially complete the polymerization reaction.
Next, in order to cool to 50 ° C. and dissolve the suspending agent, 20 mass% sulfuric acid was added.
Next, the polymerization reaction solution was passed through a 1.68 mm mesh sieve to remove aggregates, and the obtained bead polymer was washed and dehydrated and dried to obtain polymer fine particles having an average particle diameter of 0.29 mm.
Aggregates are dried in a drying oven at 80 ° C. for 12 hours, weighed, and the weight is divided by the total amount of raw material (I) and raw material (II) to measure the amount of aggregate produced (mass%). As a result, it was 0.48 mass%.
The obtained polymer fine particles were melt-kneaded using a φ30 mm twin screw extruder set at 240 ° C., and the strands were cooled and cut to obtain resin pellets. At that time, the extrusion workability was good.
The obtained pellets had a weight average molecular weight (Mw) of 118,000 and a molecular weight distribution (Mw / Mn) of 3.3.
Moreover, when the fluidity | liquidity of the obtained resin pellet was measured by MFR, it was 1.7 g / 10min.
When the tensile properties were measured, the tensile modulus was 3300 MPa, the tensile yield stress was 75 MPa, and the tensile fracture strain was 6%.
Furthermore, when Charpy impact strength (without notch) was measured as an index of impact resistance, it was 22 kJ / m ² . Moreover, when the VICAT softening temperature was measured, it was 109 degreeC and the deflection temperature under load was 100 degreeC.
Table 2 shows the monomer charge composition of weight (I) and polymer (II), the weight average molecular weight of the polymer, and the ratio of polymers (I) and (II).
Difference in time T1 from when the raw material for polymer (I) is introduced until it reaches the exothermic peak, time T2 after the raw material for polymer (II) is reached until it reaches the exothermic peak, aggregate formation amount, molecular weight The measurement results (calculated values of formula (1) and formula (2)) are shown in Table 3 below.
Further, resin pellets were produced in the same manner as in Example 1. The results of measuring the weight average molecular weight (Mw) are shown in Table 3.

In Table 2, (Mah) is a composition ratio of other vinyl monomer units copolymerizable with the methacrylic acid ester of the polymer (II).
In Table 2, (Mal) is the composition ratio of other vinyl monomer units copolymerizable with the methacrylic acid ester of the polymer (I).

When Examples and Comparative Examples were compared, it was found that when the difference in weight average molecular weight for each particle size was small as in the Examples, an acrylic resin having a good color tone was obtained.
Also, as in the examples, the relationship between the first stage polymerization time (T1) and the second stage polymerization time (T2) is T2 / T1 ≧ 1, thereby reducing the amount of aggregates produced and the difference in particle size. It turned out that the difference of the weight average molecular weight by becomes small.

[Examples 13 to 16]
Using the polymer fine particles produced in Examples 1, 2, 11, and 12, respectively, molded pieces were prepared according to the above-described (IV. Physical property measurement), and each physical property measurement was performed. The measurement results are shown in Table 5 below.

[Comparative Example 5]
2 kg of water, 65 g of tricalcium phosphate, 39 g of calcium carbonate, and 0.39 g of sodium lauryl sulfate were added to a container having a stirrer to obtain a mixed solution (A).
Next, 26 kg of water was charged into a 60 L reactor and the temperature was raised to 80 ° C., and the mixture (A), methyl methacrylate 19.5 kg, methyl acrylate 0.5 kg, lauroyl peroxide 50 g, n-octyl mercaptan 58 g Was introduced.
Thereafter, suspension polymerization was carried out while maintaining the temperature at about 80 ° C. After observing an exothermic peak, the temperature was raised to 92 ° C. at a rate of 1 ° C./min and then aged for 60 minutes to substantially complete the polymerization reaction.
Subsequently, 20 mass% sulfuric acid was added in order to cool to 50 degreeC and dissolve a suspension agent.
Next, the polymerization reaction solution was passed through a 1.68 mm mesh sieve to remove aggregates, and the obtained bead polymer was washed and dehydrated and dried to obtain polymer fine particles having an average particle diameter of 0.30 mm (Resin A).
The aggregate was dried in a drying oven at 80 ° C. for 12 hours, weighed, and the aggregate generation amount was calculated to be 0.52% by mass.
The obtained polymer fine particles were dried in a drying oven at 80 ° C. for 12 hours, followed by sieving the polymer fine particles and measuring the difference in weight average molecular weight. As described above, (III. Fine particle sieving and molecular weight measurement). ), The calculated value by the formula (1) was 0.5%, and the calculated value by the formula (2) was 0.6%.
The obtained polymer fine particles were melt-kneaded with a φ30 mm twin screw extruder set at 240 ° C., and the strands were cooled and cut to obtain resin pellets. The obtained pellet has a weight average molecular weight of 103,000, an abundance of a molecular weight component equal to or less than 1/5 of Mp is 5.3%, Mh is 2.5 mass%, and Ml is 2.5 mass. %Met.
Using the prepared polymer fine particles, molded pieces were prepared according to the above-mentioned (IV. Physical property measurement), and each physical property measurement was performed. The measurement results are shown in Table 5 below.

  When Examples 13 to 16 and Comparative Example 5 were compared, it was found that the acrylic resin according to the present invention maintained high fluidity and solvent resistance.

  The acrylic resin of the present invention is a display (device) window for mobile phones, liquid crystal monitors, liquid crystal televisions, etc., a light guide plate used in liquid crystal display, a front plate of a display device, a frame for paintings, and a window for taking in external light. , Exteriors such as signboards for display, carport roofs, sheets for display shelves, covers and gloves for lighting fixtures, molded products having secondary processing such as pressure forming, vacuum forming, blow molding, etc. It is industrially applicable as a vehicular optical component used in tail lamps, head lamps, etc., which are large and yet require durability to solvents such as alcohol-based cleaning agents, waxes and wax removers.

1 Jig 2 Molded body 3 Weight 4 Filter paper 5 Octopus thread 6 GPC elution curve 7 Baseline

The present invention relates to a method for producing acrylic resin.

Therefore, in the present invention has a high fluidity, impact resistance, the production of acrylic resin excellent acrylic resins in solvent resistance, it can be produced without causing the aggregates in the manufacturing process an object of the present invention is to provide an mETHODS.

[1]
The weight average molecular weight measured by gel permeation chromatography using a raw material mixture containing methacrylic acid ester monomer 80 to 100% by mass and acrylic acid ester monomer 20 to 0% by mass is 5,000 to 50,000. After producing the polymer (I) that is 5 to 45% by mass with respect to the entire acrylic resin,
In the presence of the polymer (I), a raw material mixture containing the methacrylic acid ester monomer and the acrylate monomer is added to obtain a polymer (II) having a weight average molecular weight of 60,000 to 350,000. And a step of producing 95 to 55% by mass with respect to the whole acrylic resin,
The time from the addition of the raw material mixture of the polymer (I) to the arrival of an exothermic peak due to polymerization exotherm is T1,
When the time from the addition of the raw material mixture of the polymer (II) to the peak temperature of the exotherm due to the polymerization exotherm is T2,
The manufacturing method of acrylic resin with which following formula (3) is satisfied.
T2 / T1 ≧ 1 (3)
[2]
The manufacturing method of the acrylic resin of Claim 1 with which following formula (4) is satisfied.
5 ≧ T2 / T1 ≧ 1 (4)
[3]
The method for producing an acrylic resin according to claim 1 or 2 , wherein the T2 is 30 minutes or more and 240 minutes or less.

Claims (12)

When sieving using a sieve based on JIS-Z8801,
A weight average molecular weight (A) of particles having a particle diameter of 500 μm or more;
A weight average molecular weight (B) of particles having a particle diameter of 355 μm to 300 μm;
A weight average molecular weight (C) of particles having a particle diameter of 150 μm or less;
And an acrylic resin that satisfies the following relational expressions (1) and (2).
0 ≦ | [(A) − (B)] / (B) | × 100 (%) ≦ 10 (1)
0 ≦ | [(C) − (B)] / (B) | × 100 (%) ≦ 10 (2) An acrylic resin comprising 80 to 99.5% by mass of methacrylic acid ester monomer units and 0.5 to 20% by mass of other vinyl monomer units copolymerizable with at least one methacrylic acid ester. ,
The weight average molecular weight measured by gel permeation chromatography (GPC) is 60,000 to 300,000,
2. The acrylic resin according to claim 1, wherein a molecular weight component of 1/5 or less of a peak molecular weight (Mp) obtained from a GPC elution curve is contained in an area area ratio of 7 to 40% obtained from the GPC elution curve. .   The acrylic resin according to claim 1 or 2, wherein the average particle size is 100 to 500 µm. A method for producing an acrylic resin according to any one of claims 1 to 3,
Using a raw material mixture containing a methacrylic ester, the polymer (I) having a weight average molecular weight of 5,000 to 50,000 measured by gel permeation chromatography is 5 to 45% by mass with respect to the whole acrylic resin. After manufacturing
In the presence of the polymer (I), a polymer (II) having a weight average molecular weight of 60,000 to 350,000 by adding a raw material mixture containing the methacrylic acid ester is 95% of the whole acrylic resin. A step of producing ~ 55% by mass,
The time from the addition of the raw material mixture of the polymer (I) to the arrival of an exothermic peak due to polymerization exotherm is T1,
When the time from the addition of the raw material mixture of the polymer (II) to the peak temperature of the exotherm due to the polymerization exotherm is T2,
The manufacturing method of acrylic resin with which following formula (3) is satisfied.
T2 / T1 ≧ 1 (3) The manufacturing method of the acrylic resin of Claim 4 with which following formula (4) is satisfied.
5 ≧ T2 / T1 ≧ 1 (4)   The method for producing an acrylic resin according to claim 4 or 5, wherein the T2 is 30 minutes or more and 240 minutes or less. Using a raw material mixture containing a methacrylic ester, the polymer (I) having a weight average molecular weight of 5,000 to 50,000 measured by gel permeation chromatography is 5 to 45% by mass with respect to the whole acrylic resin. After manufacturing
In the presence of the polymer (I), a polymer (II) having a weight average molecular weight of 60,000 to 350,000 by adding a raw material mixture containing the methacrylic acid ester is 95% of the whole acrylic resin. A step of producing ~ 55% by mass,
The time from the addition of the raw material mixture of the polymer (I) to the arrival of an exothermic peak due to polymerization exotherm is T1,
When the time from the addition of the raw material mixture of the polymer (II) to the peak temperature of the exotherm due to the polymerization exotherm is T2,
The manufacturing method of acrylic resin with which following formula (3) is satisfied.
T2 / T1 ≧ 1 (3) The manufacturing method of the acrylic resin of Claim 7 with which following formula (4) is satisfied.
5 ≧ T2 / T1 ≧ 1 (4)   The method for producing an acrylic resin according to claim 7 or 8, wherein the T2 is from 30 minutes to 240 minutes.   The acrylic resin obtained by the manufacturing method as described in any one of Claims 4 thru | or 9.   The molded object obtained by shape | molding the acrylic resin of Claim 10.   The molded article according to claim 11, which is a vehicle component.

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