JPH08225701A - Glass fiber-reinforced vinyl chloride-based resin composition - Google Patents

Abstract

PURPOSE: To obtain the subject composition containing a PVC-based polymer, a specific copolymer and glass fiber at a specific ratio, capable of providing a molding excellent in strength, impact resistance, elastic modulus, water resistance and surface appearance, excellent in moldability and useful for building members, industrial members, etc. CONSTITUTION: This composition contains (A) 100 pts.wt. PVC-based polymer, (B) 1-50 pts.wt. copolymer composed of 95-5wt.% of (X) a polymerization chain (e.g. a polymerization chain obtained by copolymerizing ethylene with propylene or a polymerization chain obtained by polymerization of propylene) which is immiscible with the component A and 5-95wt.% of (Y) a polymerization chain (e.g. a polymerization chain obtained by copolymerizing acrylonitrile with styrene or a polymerization chain obtained by polymerization of methyl methacrylate) and (C) 5-100 pts.wt. glass fiber. Furthermore, the component B is e.g. a graft copolymer or a block copolymer composed of X and Y.

Description

Detailed Description of the Invention

[0001]

TECHNICAL FIELD The present invention relates to strength, impact resistance,
Gives a molded product with excellent elastic modulus, water resistance, surface appearance, etc.
It also relates to a glass fiber reinforced vinyl chloride resin composition having excellent moldability.

[0002]

2. Description of the Related Art A vinyl chloride resin composition containing a vinyl chloride resin or a plasticizer added thereto has relatively high mechanical strength and can be manufactured at low cost. Therefore, it is used as a resin material for producing general-purpose molded products in a wide range of applications such as building members, industrial members, and electric equipment members. However, there are drawbacks such as poor heat resistance, mechanical strength, dimensional stability, and thermal expansion depending on the application.

In order to solve these drawbacks, vinyl chloride resin is filled with glass fiber to enhance its characteristics.
It is known to improve. This method generally improves rigidity and tensile strength considerably, but often reduces impact strength.

In particular, vinyl chloride resins are inferior in melt flow characteristics to other thermoplastic resins, so that wetting with glass fibers is poor, glass fibers are not uniformly dispersed, and the melting of the compound As a result of the marked deterioration of the flow properties, the glass fibers are damaged during the kneading, and the resin is thermally deteriorated, resulting in a drawback that the impact strength is particularly poor. Furthermore, since glass fibers are raised on the surface of the molded product and the surface becomes rough, the surface appearance is inferior, and it has not always been easy to obtain desired properties.

On the other hand, alloying polymers having different properties to improve the properties of the resin has been studied. For example, various proposals have been made for alloying an olefin-based resin with a styrene-based resin or a vinyl chloride-based resin (Japanese Patent Publication No. S60-36178, JP-A No. 63-604).
039, JP-A-1-165640, JP-A-2-1991.
27, JP-A-2-199128, and JP-A-2-19912.
9).

This alloyed resin has attracted attention in order to meet diversified uses, but since it uses an olefin resin, its elastic modulus and heat resistance are insufficient.

In order to eliminate the above-mentioned drawbacks, various methods have been conventionally proposed. For example, 1) a method of increasing the molding processing temperature, 2) a resin that is miscible with a lubricant, a surface modifier, or a vinyl chloride resin and has excellent flow characteristics, such as an ethylene-vinyl acetate copolymer or an ethylene-vinyl chloride copolymer. A method of lowering the viscosity of the vinyl chloride resin by adding a polymer, chlorinated polyethylene or the like to improve the wettability with the glass fiber and improve the dispersibility can be mentioned.

However, in the method 1), since the molding temperature and the decomposition temperature of the vinyl chloride resin are close to each other, strict temperature control is required, which is not practical, and a slight temperature rise occurs. As a result, the resin is decomposed and the mechanical strength of the molded product is reduced. The method 2) requires the addition of a large amount of resin in order to attain a desired viscosity level, and significantly changes the original properties of the vinyl chloride resin, and therefore has the advantage of improving the mechanical strength of the resin by adding glass fiber. It has the drawback of being offset.

Further, in order to avoid breakage of the glass fiber generated at the time of molding and to improve the mechanical strength of the molded product,
A method is known in which glass fiber is added through a vent hole or a die portion of an extruder. According to this method, the glass fiber is not damaged, but the wettability between the resin and the glass fiber is not sufficient, so that the mechanical strength, especially the water resistance is significantly impaired.

Further, in order to improve these drawbacks,
JP-B-49-6830, JP-B-49-13209 and JP-B-49-27663 polymerize vinyl monomers such as vinyl chloride, vinyl acetate and aromatic vinyl compounds in the presence of glass fibers to prepare the glass fibers as described above. A method of coating a polymer consisting of a polymer and kneading and mixing the glass fiber coated with the polymer and a vinyl chloride resin to obtain a molded article was proposed.
5427 proposes a method of improving the properties of an alloyed resin by adding a compatibilizer.

However, according to these methods, the adhesion between the resin and the glass fiber is improved, and although some improvements in the appearance of the molded product and various mechanical strengths are recognized, impact resistance,
The balance of elastic modulus, water resistance and moldability is poor, and it is not always satisfactory.

[0012]

SUMMARY OF THE INVENTION The object of the present invention is to solve the above-mentioned drawbacks of the prior art and to provide a glass fiber reinforced vinyl chloride system excellent in mechanical strength such as moldability and impact resistance and surface appearance. It is to provide a resin composition.

[0013]

Means for Solving the Problems As a result of diligent studies, the present inventor has found that the use of vinyl chloride polymers, specific copolymers and glass fibers results in mechanical properties such as impact resistance, strength, elastic modulus and water resistance. It was found that the mechanical strength is improved, the surface appearance is good, and the moldability is significantly improved. The present invention is the following invention.

A glass fiber reinforced vinyl chloride resin composition comprising the following components (A), (B) and (C) in the following proportions: (A) 100 parts by weight of vinyl chloride polymer, (B) Polymerization chain (X) 95 to 5 immiscible with vinyl chloride polymer
Copolymers 1 to 5 composed of 5% by weight and a polymerization chain (Y) 5 to 95% by weight which is miscible with the vinyl chloride polymer.
0 parts by weight, (C) 5 to 100 parts by weight of glass fiber.

[Vinyl Chloride Polymer] The vinyl chloride polymer (A) used in the present invention can be obtained by a known production method such as a suspension polymerization method, an emulsion polymerization method or a bulk polymerization method. The vinyl chloride polymer (A) preferably has an average degree of polymerization in the range of 400 to 1500, and 450 to
Those of 1000 are particularly preferable. If the average degree of polymerization is too small, mechanical properties such as impact resistance and elastic modulus, and thermal stability decrease, which is not preferable. If the average degree of polymerization is too large, the melt fluidity is significantly lowered and the molding becomes too difficult, which is not preferable.

The term "vinyl chloride polymer" as used herein means a vinyl chloride polymer substantially, and comprises 60% by weight of the constituents.
The above means that it is composed of polymerized units based on vinyl chloride. Specifically, vinyl chloride homopolymer, ethylene-vinyl chloride copolymer, vinyl acetate-vinyl chloride copolymer, a graft copolymer obtained by graft-polymerizing ethylene to a vinyl acetate-vinyl chloride copolymer, Examples thereof include chlorinated polyvinyl chloride, and these may be used alone or in combination of two or more.

[Copolymer (B)] The copolymer (B) used in the present invention has a structure having both polymerization chains (X) and (Y) in the same polymer molecule. Become. The polymerization chain (X) is a polymerization chain immiscible with the vinyl chloride polymer, and the polymerization chain (Y) is a polymerization chain miscible with the vinyl chloride polymer. The length of the polymerization chain (X) is not particularly limited as long as it is immiscible with the vinyl chloride polymer. Similarly, the length of the polymerized unit (Y) is not particularly limited as long as it is miscible with the vinyl chloride polymer.

However, a polymer obtained by alternately polymerizing the polymer units constituting the polymer immiscible with the vinyl chloride polymer and the polymer units constituting the miscible polymer is preferable as the copolymer (B). Also, a polymer in which both units are randomly polymerized is not preferable as the copolymer (B).

Therefore, as the copolymer (B), a block copolymer or a graft copolymer having at least one polymerization chain (X) and at least one polymerization chain (Y) is preferable. In the case of a graft copolymer, the polymerized chain (X) may be either a trunk chain or a branched chain, and a graft copolymer in which the polymerized chain (X) is a trunk chain and the polymerized chain (Y) is a branch chain is It is preferable in terms of the effects of the present invention and the ease of manufacturing.

In the following, a monomer which becomes a homopolymer which is immiscible with a vinyl chloride polymer is referred to as a monomer (m),
A monomer that is a homopolymer that is miscible with a vinyl chloride polymer is referred to as a monomer (n). Further, a unit derived from a monomer and constituting a polymer is called a polymerized unit, and a polymerized unit derived from a monomer (m) is a polymerized unit derived from a polymerized unit (m) and a monomer (n). The unit is called a polymerized unit (n). Further, the specific name of the polymerized unit is referred to by adding "polymerized unit" to the name of the monomer (for example, "propylene polymerized unit" and the like).

The polymerized chain (X) is preferably composed of only polymerized units (m). However, as long as it is a polymerization chain which is immiscible with the vinyl chloride polymer as a whole, the polymerization chain may contain the polymerization unit (n) or another polymerization unit. The other polymerized units include a monomer (m)
And those other than the monomer (n) and those which are difficult to distinguish from any of them. The polymerized chain (X) may be composed of two or more kinds of polymerized units (m), and the same applies when it has a polymerized unit (n) or another polymerized unit.

Similarly, the polymerized chain (Y) is a polymerized unit (n).
The polymer chain may have a polymer unit (m) or another polymer unit as described above, as long as the polymer chain has a miscibility with the vinyl chloride polymer as a whole. May be. Further, each polymerized unit may include two or more kinds.

The term "miscible" as used herein means that a vinyl chloride polymer and a miscible polymer are mixed in a molecular order in a thermodynamically stable state, or some affinity is exerted on the interface to stabilize the stability. It means the property of being in a microphase-separated state. Therefore, since the copolymer (B) has the polymerization chain (X) and the polymerization chain (Y) in the same molecule, for example, in the continuous layer of the vinyl chloride polymer, the particle size is 0.1 to 10
It can be stably dispersed in a particle state of 0 μm.

Polymerization chain (X) constituting the copolymer (B)
And the polymerized chain (Y), the former is 95 to 5% by weight,
The latter is in the range of 5 to 95% by weight and the former is 80 to 20%.
A range of 20% to 80% by weight, the latter being 20% by weight, is particularly preferable.

If the polymerization chain (X) is less than 5% by weight, the melt flow characteristics of the vinyl chloride polymer cannot be improved, so that there is no effect in improving the moldability of the composition, and the surface appearance is improved. Does not arrive. If it exceeds 95% by weight, it is poorly miscible with the vinyl chloride polymer, so that it is not sufficiently dispersed in the matrix vinyl chloride polymer, and the adhesive strength at the interface with the vinyl chloride polymer is not strong. Therefore, the mechanical strength of the obtained molded article is reduced.

The molecular weight of the copolymer (B) is not particularly limited, and the average molecular weight is preferably 1,000 to 400,000.
2000-200000 is especially preferable.

[Specific Examples of Polymerized Chain (X)] As described above, the polymerized chain (X) is a chain containing polymerized units (m). The polymerized unit (m) is formed by polymerizing the monomer (m). A relatively small amount of the monomer (n) or another monomer may be copolymerized with the monomer (m). As the polymerized chain (X), a polymerized chain formed substantially only of one or more kinds of monomers (m) is preferable.

The monomer (m) is not limited as long as it gives a polymer which is substantially immiscible with the vinyl chloride polymer, and is not limited to an olefin monomer and an aromatic vinyl monomer. There is a body etc. As the monomer for forming the polymerized chain (X), an olefinic monomer is particularly suitable.

Preferable examples include ethylene, propylene and other α-olefin type homopolymers or a combination of these monomers. Specifically, ethylene, propylene, butadiene, a combination of ethylene-propylene, a combination of propylene-butylene and the like are suitable as the monomer for forming the polymerization chain (X). Of these, ethylene and propylene are preferable, and propylene is particularly preferable.

[Specific Example of Polymerized Chain (Y)] The polymerized chain (Y) is a chain containing polymerized units (n). The polymerized unit (n) is formed by polymerizing the monomer (n),
The monomer (m) or another monomer may be copolymerized with the monomer (n). The monomer (n) is not limited as long as it gives a polymer that is substantially miscible with a vinyl chloride polymer, and an acrylic acid-based monomer such as an acrylic acid alkyl ester-based monomer. , Methacrylic acid-based monomers such as methacrylic acid alkyl ester-based monomers, and vinyl cyanide-based monomers.

The vinyl cyanide-based monomer forms a polymer having a high miscibility with the vinyl chloride-based polymer, but the polymer alone is insufficient in physical properties, and therefore, it cannot be mixed with other monomers. It is preferable to polymerize to form a polymerized chain (Y).

As the monomer to be copolymerized with the vinyl cyanide monomer, the monomer (m) can be used, and the aromatic vinyl monomer is particularly preferable. As the monomer forming the polymerization chain (Y), a combination of vinyl cyanide-based monomer-aromatic vinyl-based monomer and alkyl methacrylic acid-based monomer are particularly preferable.

Examples of the vinyl cyanide-based monomer include acrylonitrile and methacrylonitrile, and examples of the aromatic vinyl-based monomer include styrene and α-.
Methylstyrene, vinyltoluene, chlorostyrene, etc. As the combination of the vinyl cyanide-based monomer and the aromatic vinyl-based monomer, the combination of acrylonitrile-styrene is particularly preferable.

In the polymerized units (Y) composed of vinyl cyanide-based monomer and aromatic vinyl-based monomer, the proportion of vinyl cyanide-based polymerized units is preferably 5% by weight or more in the polymerization chain (Y), A range of 10 to 50% by weight is particularly preferred.
When the proportion of vinyl cyanide-based polymer units is low, the copolymerization chain (Y) is poorly miscible with the vinyl chloride-based polymer, and therefore the copolymer (B) is sufficiently dispersed in the vinyl chloride-based polymer as the matrix. First of all, the mechanical strength of the obtained molded article decreases, and the affinity with glass fiber is not sufficient, so that the water resistance of the obtained molded article deteriorates.

As an example of the alkyl methacrylate ester-based monomer, an alkyl methacrylate monomer having an alkyl moiety having 4 or less carbon atoms such as methyl methacrylate and ethyl methacrylate is preferable, and methyl methacrylate is particularly preferable. preferable.

As the monomer for forming the polymerization chain (Y), one or more kinds of the methacrylic acid alkyl ester-based monomers, the methacrylic acid alkyl ester-based monomer and other methacrylic acid alkyl ester-based monomers are used. A combination with a monomer and a combination of the methacrylic acid alkyl ester-based monomer and a monomer other than the methacrylic acid alkyl ester-based monomer are preferable. Particularly preferred are those consisting essentially of methyl methacrylate polymer units.

The method for producing the copolymer (B) is not particularly limited, and conventionally known methods can be adopted. For example, a radical-generating agent such as benzoyl peroxide and dikurumi peroxide is used in a polymer obtained by polymerizing one or more kinds of monomers (m), and the monomers ( A method of reacting at least one of n) to obtain a graft copolymer can be mentioned. For the polymerization reaction, a solvent such as toluene or xylene can be used if necessary.

In addition, a method in which one or more monomers (m) are subjected to living polymerization and then one or more monomers (n) are subsequently reacted to directly obtain a block copolymer, Or
A polymer obtained by polymerizing at least one kind of the monomer (m) and a polymer obtained by polymerizing at least one kind of the monomer (n) are separately polymerized, and a carboxyl group is provided at one end of each polymer. Alternatively, there may be mentioned a method of obtaining a copolymer (B) by reacting a polymer modified by introducing an isocyanate group and a hydroxyl group or an amino group into the other, and modifying the polymer.

The blending ratio of the copolymer (B) in the present invention is 1 to 5 with respect to 100 parts by weight of the vinyl chloride polymer.
It is 0 part by weight, particularly preferably 5 to 25 parts by weight. If it is less than 1 part by weight, the object cannot be achieved, and if it exceeds 50 parts by weight, the original properties of the vinyl chloride polymerization chain are changed.

[Glass Fiber] As the glass fiber, various commercially available forms, for example, chopped strand-like or roving-like glass fibers are used. It is preferable in terms of handling that these glass fibers have a length of 1 to 50 mm, and more preferable length is 1 to 20 m.
m. The glass fiber diameter is preferably 1 to 20 μm.

Further, the glass fiber is a coupling agent,
The film may be surface-treated with a film former, a lubricant, or other surface-treating agent. For example, the coupling agent includes a silane compound having a hydrolyzable group bonded to a silicon atom, which is called a silane coupling agent. Specific examples of the silane coupling agent include the following compounds.

Acrylic silane compounds such as γ-methacryloxypropyltriethoxysilane and γ-methacryloxypropylmethyldiethoxysilane, epoxysilane compounds such as γ-glydoxypropyltrimethoxysilane, and γ-aminopropyltriethoxysilane. , N-β
-Aminosilane compounds such as aminoethyl-γ-aminopropyltriethoxysilane, vinylsilane compounds such as vinyltrimethoxysilane, and chlorosilane compounds such as γ-chloropropyltrimethoxysilane.

The filling amount of the glass fiber is 5 to 100 parts by weight based on 100 parts by weight of the vinyl chloride polymer. If it is less than 5 parts by weight, the purpose of strengthening and improving various properties of the vinyl chloride resin cannot be achieved, and if it exceeds 100 parts by weight, the glass fiber addition efficiency is not so improved, and conversely the moldability is extremely lowered.

[Other compounding agents, etc.] The glass fiber reinforced vinyl chloride resin composition of the present invention is preferably used as a molding composition for molding. That is, it is provided for molding alone or by adding various compounding agents. Examples of the method for molding the glass fiber reinforced vinyl chloride resin composition include injection molding, extrusion molding, press molding, calendering and the like which are generally applied to thermoplastic resins. Specifically, each powder or pellet of the composition is blended by using a Henschel mixer or the like, and is blended with a single-screw or twin-screw extruder to 150 to 18
Melt kneading at 0 ° C. to obtain a molded product. In particular, it is used for producing a molded product by extrusion molding.

The glass fiber reinforced vinyl chloride resin composition of the present invention contains various known compounding agents, that is, stabilizers for vinyl chloride resin, impact modifiers, lubricants, pigments, antistatic agents, and anti-aging agents. Agents, fillers, foaming agents, flame retardants and the like can be added as necessary. The following can be illustrated as a typical thing of these compounding agents.

Organic tin heat stabilizers such as dibutyltin dilaurate and dibutyltin distearate; stabilizers of aliphatic carboxylic acid salts such as barium stearate, calcium stearate and zinc stearate; inorganic stabilizers; and epoxidized soybean oil. Stabilizers such as epoxy compounds, organic phosphates and organic phosphites, impact modifiers such as MBS resins and acrylic rubbers, waxes, metal soaps, stearic acid, lubricants such as higher fatty acids, and phenol-based antioxidants. Oxidizing agents, phosphite stabilizers, anti-aging agents such as UV absorbers, fillers such as carbon black, hydrated calcium silicate, silica, talc and calcium carbonate.

The total amount of these compounding agents, excluding the filler, is preferably 50 parts by weight or less with respect to 100 parts by weight of the vinyl chloride polymer. Further, the total amount of these compounding agents including the filler is preferably 100 parts by weight or less based on 100 parts by weight of the vinyl chloride polymer.

The shape of the molded product of the glass fiber reinforced vinyl chloride resin composition of the present invention is not particularly limited, and it is preferably an extrusion molded product such as a plate-shaped product, a rod-shaped product or a tubular product having various sectional shapes. . In addition, as its use, rain gutter, eaves,
Examples of building materials include outer wall siding materials and window frames.

[0049]

[Examples] The present invention will be specifically described below with reference to Examples (Examples 1 to 6) and Comparative Examples (Examples 7 to 9), but the present invention is not limited thereto. In addition, a part says a weight part.

[Example 1] [Preparation of vinyl chloride polymer A1] Partially saponified polyvinyl alcohol (Gosenol KH manufactured by Nippon Synthetic Chemical Industry Co., Ltd.)
-20) 3 parts, azobisisobutyronitrile 0.5 part,
Then, 3000 parts of pure water was added into a separately prepared pressure reaction type reactor, and after replacement with nitrogen gas, 1000 parts of vinyl chloride was charged. After reacting at 65 ° C. for 6 hours, the unreacted monomer was recovered and then dehydrated and dried to obtain a powdery polymer 9
50 parts were obtained. The degree of polymerization of the obtained polymer was 800. Hereinafter, this is referred to as vinyl chloride polymer A1.

[Preparation of Copolymer (B)] 60 parts of polypropylene having a melt flow index of 9 g / 10 min, Irganox 1010 (antioxidant manufactured by Ciba-Geigy)
170 parts of 0.1 part, 1 part of dicumyl peroxide, 10 parts of acrylonitrile and 30 parts of styrene under nitrogen atmosphere
Polymerization was carried out at 0 ° C for 2 hours. After the completion of the polymerization, it was thoroughly washed with acetone and dried to obtain a copolymer B1.

The resulting copolymer B1 was a graft copolymer composed of a chain of propylene polymer units and a copolymer chain of acrylonitrile polymer units-styrene polymer units. 70 chains of propylene polymer units
The copolymerization chain consisting of the acrylonitrile polymer unit and the styrene polymer unit was 30% by weight, and the weight ratio of the acrylonitrile polymer unit and the styrene polymer unit was 28/72.

[Preparation, molding and evaluation of composition] 100 parts of vinyl chloride polymer A1, dibutyltin mercaptide 3
Parts, 0.5 parts of stearic acid, 10 parts of copolymer B1 and 27.5 parts of chopped strand glass fibers having a length of 3 mm and a fiber diameter of 13 μm were mixed and blended using a Henschel mixer.

Then, using a 30 mm single-screw extruder with L / D = 24 and compression ratio = 3.1, the cylinder temperature was 180 ° C.,
Die temperature 165 ° C, rotation speed 7.8 rpm, thickness 3 m
A flat plate having a width of m and a width of 30 mm was extruded. The extrusion moldability, the surface appearance of the obtained flat plate, and various physical properties were evaluated and measured by the methods described below. The results are shown in Table 1.

Extrudability: Evaluated by screw load (unit: ampere) and discharge rate (unit: g / min). Tensile strength (unit: 10 ³ kg / cm ² ) and tensile modulus (unit: 10 ⁴ kg / cm ² ): JIS K7113
Complies with. Flexural strength (unit: 10 ³ kg / cm ² ) and flexural modulus (unit: 10 ⁴ kg / cm ² ): JIS K7203
Complies with. Izod impact strength (with notch) (Unit: kg / cm
/ Cm ² ): According to JIS K7110. Heat distortion temperature (unit: ° C): conforming to JIS K7207 (load 18.5 kg / cm ² ). Water resistance: Evaluated by the tensile strength retention rate (unit:%) after the flat plate molded article was immersed in warm water at 50 ° C. for 7 days. Surface appearance: 3 stages by visual observation (○: No unevenness in surface gloss, roughening, no swelling. Δ: Unevenness in surface glossiness, or roughening, swelling. ×: unevenness in surface glossiness, roughening, swelling.) Evaluated by.

Example 2 A graft copolymer B2 was obtained by the same production method as in Example 1 except that the charging ratio and charging amount of acrylonitrile and styrene were changed. The graft copolymer B2 thus obtained had 50% by weight of chains consisting of propylene polymerized units and 50% by weight of copolymerized chains of acrylonitrile polymerized units-styrene polymerized units, of which the weight of acrylonitrile polymerized units and styrene polymerized units was The ratio was 25/75.

A flat plate molded article was prepared in the same manner as in Example 1 except that the copolymer B2 was used in place of the copolymer B1 and various evaluations were carried out. Table 1 shows the results.

Example 3 Instead of polypropylene, ethylene having a polymerization ratio of ethylene and propylene of 50/50 was used.
Copolymer B of Example 1 except that a propylene copolymer was used
Graft copolymer B3 was obtained by the same production method as in 1. The graft copolymer B3 thus obtained contained 70% by weight of a copolymerized chain consisting of ethylene polymerized units-propylene polymerized units and 30% by weight of a copolymerized chain consisting of acrylonitrile polymerized units-styrene polymerized units, of which acrylonitrile polymerized units and styrene were contained. The weight ratio with the polymerized units was 26/74.

A flat plate molded article was prepared in the same manner as in Example 1 except that the copolymer B3 was used in place of the copolymer B1, and various evaluations were carried out. Table 1 shows the results.

Example 4 Example 1 except that 40 parts of methyl methacrylate was used instead of acrylonitrile and styrene.
Graft copolymer B4 was obtained by the same method as described above. In the obtained graft copolymer B4, the chain consisting of propylene polymer units was 70% by weight and the chain consisting of a methyl methacrylate polymer was 30% by weight.

A flat plate molded article was prepared in the same manner as in Example 1 except that the copolymer B4 was used in place of the copolymer B1 and various evaluations were carried out. Table 1 shows the results.

Example 5 25 parts of acrylonitrile, 75 parts of styrene, 3 parts of 2-mercaptoethanol and 0.5 part of benzoyl peroxide were dissolved in 300 parts of xylene and polymerized at 65 ° C. for 5 hours to give hydroxyl groups at the ends. An acrylonitrile-styrene copolymer having the above was obtained. 30 parts of this polymer and 70 parts of a commercially available terminal carboxyl-modified propylene polymer (MPX-1001 manufactured by Sanyo Kasei Co., Ltd.) were dissolved in 100 parts of xylene and then reacted at 150 ° C. for 3 hours,
A block copolymer B5 was obtained.

The block copolymer B5 thus obtained contained 70% by weight of a chain of propylene polymerized units and 3 of a chain of acrylonitrile polymerized units-styrene polymerized units.
It was 0 polymerization%, and the weight ratio of the acrylonitrile polymer unit and the styrene polymer unit was 28/72.

A flat plate molded article was prepared and various evaluations were carried out in the same manner as in Example 1 except that the copolymer B5 was used in place of the copolymer B1. Table 1 shows the results.

[Example 6] The same method as in Example 5 was repeated except that the charging ratio of the acrylonitrile-styrene copolymer having a hydroxyl group at the terminal and the terminal carboxyl-modified propylene polymer (MPX-1001 manufactured by Sanyo Kasei Co., Ltd.) was changed. A block copolymer B6 was obtained. The obtained block copolymer B6 had a chain of propylene polymer units of 50% by weight and a copolymer chain of acrylonitrile polymer units-styrene polymer units of 50% by weight. The weight ratio of the acrylonitrile polymer units to the styrene polymer units was 50% by weight. Was 28/72.

A flat plate molded article was prepared in the same manner as in Example 1 except that the copolymer B6 was used in place of the copolymer B1 and various evaluations were carried out. Table 1 shows the results.

[Example 7] 100 of vinyl chloride polymer A1
Parts, dibutyltin mercaptide 3 parts, stearic acid 0.5
Parts and 25 parts of chopped strand glass fibers having a length of 3 mm and a fiber diameter of 13 μm were mixed and blended using a Henschel mixer. Hereinafter, a flat plate molded article was prepared in the same manner as in Example 1 and various evaluations were performed. Table 1 shows the results.

Example 8 280 parts of chopped strand glass fiber having a length of 3 mm and a fiber diameter of 13 μm was sufficiently impregnated with a mixed solution of 40 parts of acrylonitrile, 60 parts of styrene and 1 part of benzoyl peroxide, and then water 1800 was added.
Parts were added and polymerization was carried out at 80 ° C. for 5 hours. After completion of the polymerization, the product was thoroughly washed with water and dried at 60 ° C.

The glass fiber obtained was acrylonitrile-
The glass fiber was coated with a styrene copolymer, and the glass fiber content was 80% by weight, and the weight ratio of the acrylonitrile polymer unit and the styrene polymer unit was 28/72.
Hereinafter, this is referred to as AS resin-coated glass fiber.

In Example 1, the copolymer B1 was not used, and the AS resin-coated glass fiber was replaced with 33.
A flat plate molded article was prepared and various evaluations were performed in the same manner as in Example 1 except that 3 parts were used. Table 1 shows the results.

[Example 9] 10 of the copolymer B1 in Example 1
7 parts polypropylene, acrylonitrile-
A flat plate molded article was prepared in the same manner as in Example 1 except that 3 parts of a styrene copolymer (weight ratio of acrylonitrile polymerized units to styrene polymerized units 28/72) was used, and various evaluations were performed. Table 1 shows the results.

From Table 1, it can be seen that the tensile strength, the tensile elastic modulus, the bending elastic modulus, and the water resistance of the examples are all superior to those of the comparative examples. In particular, the effect of improving impact strength is high, and it exhibits extremely excellent mechanical properties. Further, it has excellent moldability and surface appearance.

[0073]

[Table 1]

[0074]

INDUSTRIAL APPLICABILITY The glass fiber reinforced vinyl chloride resin composition of the present invention is produced by using the copolymer (B) composed of the polymerization chain (X) and the polymerization chain (Y). (X) significantly improves the melting characteristics of the vinyl chloride resin by the sliding action, and also enhances the dispersibility of the vinyl chloride polymer, which is the matrix resin, by the polymerization chain (Y) and strengthens the interfacial adhesion with the glass fiber. The effect of significantly improving strength, impact resistance, elastic modulus, water resistance, surface appearance and moldability is exerted by the synergistic effect of.

 ─────────────────────────────────────────────────── --- Continuation of the front page (72) Inventor Tomiya Sugiura 1150 Hazawa-machi, Kanagawa-ku, Yokohama, Kanagawa Prefecture Central Research Laboratory, Asahi Glass Co., Ltd.

Claims (5)

[Claims] 1. A glass fiber reinforced vinyl chloride resin composition comprising the following components (A), (B) and (C) in the following proportions. (A) 100 parts by weight of vinyl chloride polymer, (B) Polymerization chain (X) 95 to 5 immiscible with vinyl chloride polymer
Copolymers 1 to 5 composed of 5% by weight and a polymerization chain (Y) 5 to 95% by weight which is miscible with the vinyl chloride polymer.
0 parts by weight, (C) 5 to 100 parts by weight of glass fiber. 2. The composition according to claim 1, wherein the copolymer (B) is a graft copolymer or a block copolymer composed of a polymer chain (X) and a polymer chain (Y). 3. The polymerization chain (X) is a polymerization chain in which an olefinic monomer is polymerized, and the polymerization chain (Y) is a copolymerization chain in which a vinyl cyanide monomer and an aromatic vinyl monomer are copolymerized. The composition according to claim 1 or 2, which is a polymerization chain or a polymerization chain in which an alkyl methacrylic acid ester monomer is polymerized. 4. The composition according to claim 1, 2 or 3, wherein the polymer chain (X) is a polymer chain in which ethylene and propylene are copolymerized or a polymer chain in which propylene is polymerized. 5. The composition according to claim 1, 2, 3 or 4, wherein the polymer chain (Y) is a polymer chain in which acrylonitrile and styrene are copolymerized or a polymer chain in which methyl methacrylate is polymerized.