JP2004285334A - Rubber-modified impact-resistant resin composition - Google Patents

Abstract

<P>PROBLEM TO BE SOLVED: To provide an impact-resistant polystyrene resin composition improved in cold flow properties of a rubber and well-balancedly improved simultaneously in reactivity with a styrene monomer, impact resistance, gloss performances, tensile strength and tensile elongation performances, low-temperature characteristics and the like. <P>SOLUTION: The rubber-modified impact-resistant styrenic resin composition comprises a rubbery polymer, where the rubbery polymer is a modified polybutadiene obtained by modifying a high cis-high vinyl polybutadiene in the presence of a transition metal catalyst and has the ratio (T-cp/ML<SB>1+4</SB>) of a 5% toluene solution viscosity (T-cp) measured at 30°C to the Mooney viscosity (ML<SB>1+4</SB>) at 100°C within the range of 0.5-3.5 and a cold flow rate (CF) of less than 20 mg/min. <P>COPYRIGHT: (C)2005,JPO&NCIPI

Description

The present invention relates to a rubber-modified impact-resistant polystyrene resin having improved impact resistance and other properties in a well-balanced manner.

Copolymers obtained by radical polymerization of styrene monomer with addition of polybutadiene are widely known as impact-resistant polystyrene resins having improved impact resistance in addition to the excellent properties of polystyrene. As the rubber modifier used for producing this impact-resistant polystyrene resin, generally, a cis-1,4 structure obtained by polymerizing 1,3-butadiene using alkyllithium as a catalyst has a content of 30 to 35%, Polymerization of 1,3-butadiene with a low cis polybutadiene (hereinafter, low cis BR) having a vinyl structure of 10 to 20% and a trans-1,4 structure of 50 to 60% and a cobalt, titanium or nickel catalyst. There is a high cis polybutadiene (hereinafter, high cis BR) having a cis-1,4 structure of 90 to 98%, a vinyl structure of 1 to 5%, and a trans-1,4 structure of 1 to 5%. .

  On the other hand, according to the present applicant, for example, JP-A-10-139835 (Patent Document 1), JP-A-10-152535 (Patent Document 2), JP-A-10-218949 (Patent Document 3), In Japanese Patent Application Publication No. 10-273574 (Patent Document 4) and the like, as a rubber modifier, a metallocene catalyst having a cis-1,4 structure of 65 to 95% and a 1,2 structure of 30 to 4% was produced. An impact-resistant polystyrene resin using high cis-high vinyl BR (hereinafter, HC-HVBR) has been reported.

High cis BR is characterized by low glass transition temperature (usually -95 to -110 ° C) and thus excellent in low-temperature properties, but low reactivity with styrene monomer (graft ratio) due to low vinyl structure content, Impact-resistant polystyrene resin obtained by using high cis BR is excellent in Izod impact resistance, but can be sufficiently satisfied in terms of rubber particle size reduction (glossy) and surface impact resistance (DuPont impact resistance). is not. On the other hand, low cis BR has a high glass transition temperature (usually -75 to -95 ° C), high reactivity with styrene monomer (graft ratio) due to high vinyl structure content, and is obtained using low cis BR. Although the impact-resistant polystyrene resin obtained has a small rubber particle size and excellent surface impact resistance, it is not sufficiently satisfactory in Izod impact resistance and low-temperature characteristics.

On the other hand, by using a high cis-high vinyl BR (hereinafter, HC-HVBR) for rubber for impact-resistant polystyrene, development of a BR that retains the characteristics of high cis BR and the characteristics of low cis BR has been promoted. It is strongly desired. The reactivity with the styrene monomer due to the high vinyl structure is equivalent to that of the low cis BR, and the impact-resistant polystyrene resin obtained by using the HC-HVBR has excellent gloss and surface impact and a high cis-BR. A rubber-modified impact-resistant polystyrene resin having both conventional high cis BR and low cis BR characteristics, which is excellent in Izod impact resistance and low-temperature characteristics due to the low glass transition temperature derived from the 1,4 structure content, can be obtained. It is disclosed.
However, depending on conditions such as the composition, it may be difficult to control the reactivity with the styrene monomer and the rubber particle diameter, etc., and from the viewpoint of improving various physical properties such as the impact resistance balance of the impact-resistant styrene resin composition. In some cases, improvement was desired.

  In addition, the high cis-high vinyl BR (hereinafter, HC-HVBR) produced with the above-mentioned metallocene catalyst has a microstructure having a moderate 1,2-structure in the high cis structure, a small trans structure, and a molecular linearity. Although it is a polybutadiene having a high (linearity), it shows a relatively high cold flow, so that improvement in storage and transportation may be required in some cases.

JP-A-10-139835 JP-A-10-152535 JP-A-10-218949 JP-A-10-273574

The present invention provides an impact-resistant polystyrene resin that improves the cold flow property of rubber, and simultaneously improves the reactivity with styrene monomer, impact resistance, gloss performance, tensile strength and tensile elongation performance, and low-temperature properties in a well-balanced manner. It is intended to provide a composition.

The present invention provides a rubber-modified impact-resistant styrenic resin composition containing a rubbery polymer,
The rubbery polymer is a high cis-high vinyl polybutadiene, a modified polybutadiene obtained by modification in the presence of a transition metal catalyst, and a 5% toluene solution viscosity (T-cp) measured at 30 ° C. and 100 ° C. Modified polybutadiene having a ratio (T-cp / ML _{1 + 4} ) to the Mooney viscosity (ML _{1 + 4} ) in the range of 0.5 to 3.5 and a cold flow rate (CF) of less than 20 mg / min. And a rubber-modified impact-resistant styrenic resin composition characterized by using

  Further, it is preferable that unmodified high cis-high vinyl polybutadiene is produced by a metallocene catalyst.

  The modified polybutadiene preferably has a cis-1,4 structure of 65 to 95% and a vinyl structure of 30 to 4%.

  The modified polybutadiene preferably has an intrinsic viscosity of 0.5 to 7 measured in toluene at 30 ° C.

  Further, the metallocene catalyst is preferably a catalyst comprising (A) a metallocene complex of a transition metal compound, and (B) an ionic compound of a non-coordinating anion and a cation and / or an alumoxane.

  Further, the rubbery polymer preferably comprises 1 to 25% by weight and the styrene resin composition 99 to 75% by weight.

According to the present invention, it is possible to improve various properties such as an impact resistance balance of an impact-resistant styrene resin composition by improving reactivity with a styrene monomer and control of a rubber particle diameter.

  The high cis-high vinyl polybutadiene of the present invention will be described. The high cis-high vinyl polybutadiene rubber (HC-HVBR) preferably has a cis-1,4-structural unit content in the microstructure of 65 to 95 mol%, particularly preferably 70 to 90 mol%, and preferably The 1,2-structural unit content is 4 to 30 mol%, particularly preferably 5 to 25 mol%, and more preferably 7 to 15 mol%. Further, the content of the trans-1,4-structural unit is preferably 5 mol% or less, particularly preferably 0.5 to 4.0 mol%.

Further, it is preferable that the relational expression between the 5% toluene solution viscosity (T-cp) of HC-HVBR at 25 ° C. and the Mooney viscosity (ML _{1 + 4} ) at 100 ° C. satisfies the following expression (I).
0.5 ≦ T-cp / ML _{1 + 4} ≦ 3.5. . . (I)
Particularly preferably, 2 ≦ T-cp / ML _{1 + 4} ≦ 3.5 is satisfied.

  Further, the toluene solution viscosity (Tcp) of HC-HVBR is preferably from 20 to 500, and particularly preferably from 30 to 300.

The Mooney viscosity (ML _{1 + 4} ) of the HC-HVBR of the present invention is preferably from 10 to 200, particularly preferably from 25 to 100.

  The molecular weight of HC-HVBR is preferably from 0.1 to 10, particularly preferably from 0.1 to 3, as the intrinsic viscosity [η] measured in toluene at 30 ° C.

Further, the molecular weight of HC-HVBR is preferably in the following range as the molecular weight in terms of polystyrene.
Number average molecular weight (Mn): 0.2 × 10 ⁵ to 10 × 10 ⁵ , more preferably 0.5 × 10 ^{5 to} 5 × 10 ⁵
Weight average molecular weight (Mw): 0.5 × 10 ^{5 to} 20 × 10 ⁵ , more preferably 1 × 10 ⁵ to 10 × 10 ⁵

  Moreover, the molecular weight distribution (Mw / Mn) of the HC-HVBR of the present invention is preferably 1.5 to 3.5, more preferably 1.6 to 3.

The above HC-HVBR is, for example,
It can be produced by polymerizing butadiene using (A) a metallocene complex of a transition metal compound, and (B) a catalyst obtained from an ionic compound of a non-coordinating anion and a cation and / or an aluminoxane.

Alternatively, (A) a metallocene complex of a transition metal compound,
(B) an ionic compound of a non-coordinating anion and a cation,
(C) an organometallic compound of an element of Groups 1 to 3 of the periodic table, and
(D) Water
Can be produced by polymerizing butadiene using a catalyst obtained from

  Examples of the metallocene complex of the transition metal compound (A) include metallocene complexes of transition metal compounds of Groups 4 to 8 of the periodic table.

For example, a metallocene complex of a transition metal belonging to Group 4 of the periodic table such as titanium or zirconium (for example, CpTiCl ₃ ), a metallocene complex of a transition metal belonging to Group V of the periodic table such as vanadium, niobium, or tantalum; Group 6 transition metal metallocene-type complexes, and metallocene type complexes of Group VIII transition metals such as cobalt and nickel are exemplified.

  Among them, a metallocene complex of a transition metal of Group 5 of the periodic table is preferably used.

Examples of the metallocene complex of the transition metal compound of Group V of the periodic table include:
(1) RM · La, that is, a transition metal compound of Group 5 of the Periodic Table having an oxidation number of +1 having a ligand of a cycloalkadienyl group (2) R _n MX _2-n · La, ie, at least one Transition metal compound belonging to Group 5 of the periodic table having an oxidation number of +2 and having a ligand of a cycloalkadienyl group of the formula (3): R _n MX _3-n · La
(4) RMX ₃・ La
(5) RM (O) X ₂・ La
(6) R _n MX _3-n (NR ′)
(Wherein n is 1 or 2, a is 0, 1 or 2).

Among _{them, RM · La, R n MX} 2-n · La, R 2 M · La, RMX 3 · La, etc. RM (O) X ₂ · La are preferably exemplified.

  M is preferably a transition metal compound of Group 5 of the periodic table.

As the metallocene complex of the transition metal compound (A) of Group 5 of the periodic table, a vanadium compound in which M is vanadium is preferable. For example, RV · La, RVX · La , R 2 M · La, RMX 2 · La, RMX 3 · La, etc. RM (O) X ₂ · La are preferably exemplified. Particularly, RV · La and RMX ₃ · La are preferred.

Specific examples of the compound represented by RMX ₃ .La include the following. Cyclopentadienyl vanadium trichloride is exemplified.

Specific compounds represented by RM (O) X ₂ include cyclopentadienyloxovanadium dichloride, methylcyclopentadienyloxovanadium dichloride, benzylcyclopentadienyloxovanadium dichloride, (1,3-dimethylcyclohexane). (Pentadienyl) oxovanadium dichloride.

  Examples of the non-coordinating anion constituting the ionic compound of the non-coordinating anion and the cation as the component (B) include, for example, tetra (phenyl) borate and tetra (fluorophenyl) borate. Can be

  On the other hand, examples of the cation include a trisubstituted carbonium cation such as a triphenylcarbonium cation.

  Further, alumoxane may be used as the component (B). The alumoxane is obtained by contacting an organic aluminum compound with a condensing agent, and includes a chain aluminoxane represented by the general formula (-Al (R ') O-) n or a cyclic aluminoxane. (R ′ is a hydrocarbon group having 1 to 10 carbon atoms, including those partially substituted with a halogen atom and / or an alkoxy group. N is the degree of polymerization and is 5 or more, preferably 10 or more.) . Examples of R ′ include a methyl, ethyl, propyl, and isobutyl group, and a methyl group is preferable.

  The conjugated diene may be polymerized by combining the component (A) and the component (B) with an organometallic compound of a Group 1 to 3 element of the periodic table as the component (C). The addition of the component (C) has the effect of increasing the polymerization activity. Examples of the organometallic compounds of Group 1 to 3 elements of the periodic table include organoaluminum compounds, organolithium compounds, organomagnesium compounds, organozinc compounds, and organoboron compounds.

As the combination of each of the above catalyst components, RMX ₃ such as cyclopentadienyl vanadium trichloride (CpVCl ₃ ) or RM such as cyclopentadienyl oxovanadium dichloride (CpV (O) Cl ₂ ) as component (A) A combination of (O) X ₂ and triphenylcarbenium tetrakis (pentafluorophenyl) borate as the component (B) and a trialkylaluminum such as triethylaluminum as the component (C) are preferably used.

When an ionic compound is used as the component (B), the above alumoxane may be used in combination as the component (C).
The order of adding the catalyst components is not particularly limited.

  In the present invention, it is preferable to further add water as the component (D) as the catalyst system. The molar ratio (C) / (D) of the organoaluminum compound of the component (C) to water of the component (D) is preferably from 0.66 to 5, more preferably from 0.7 to 1.5. .

  At the time of polymerization, hydrogen can be allowed to coexist if necessary.

  Here, the butadiene monomer to be polymerized may be a whole or a part. In the case of some of the monomers, the contact mixture described above can be mixed with the remaining monomer or the remaining monomer solution.

  The polymerization method is not particularly limited, and solution polymerization or bulk polymerization using 1,3-butadiene itself as a polymerization solvent can be applied. Aromatic hydrocarbons such as toluene, benzene and xylene, aliphatic hydrocarbons such as n-hexane, butane, heptane and pentane, alicyclic hydrocarbons such as cyclopentane and cyclohexane, 1-butene and 2-butene Examples include hydrocarbon solvents such as olefin hydrocarbons, mineral spirits, solvent naphtha, and kerosene, and halogenated hydrocarbon solvents such as methylene chloride.

  Further, a mixture of a low molecular weight HCHV component and a high molecular weight HCHV component may be used.

As a method of adjusting the molecular weight in the present invention, there is a method of polymerizing a conjugated diene compound in the presence of a chain transfer agent such as hydrogen using the above-mentioned catalyst.

  After the polymerization reaction achieves a predetermined polymerization rate, a transition metal catalyst is added and reacted to modify the polymer chain.

  Examples of the transition metal compound in the transition metal catalyst include a titanium compound, a zirconium compound, a vanadium compound, a chromium compound, a manganese compound, an iron compound, a ruthenium compound, a cobalt compound, a nickel compound, a palladium compound, a copper compound, a silver compound, and a zinc compound. No. Among them, a cobalt compound is particularly preferable.

  The transition metal catalyst of the present invention is preferably a system comprising a transition metal compound, organoaluminum, and water.

  As the cobalt compound, a salt or complex of cobalt is preferably used. Particularly preferred are cobalt salts such as cobalt chloride, cobalt bromide, cobalt nitrate, cobalt octylate, cobalt naphthenate, cobalt versatate, cobalt acetate, cobalt malonate, and bisacetylacetonate and trisacetylacetonate of cobalt. And organic base complexes such as triarylphosphine complex, trialkylphosphine complex, pyridine complex and picoline complex of cobalt acetoacetate and cobalt halide, and ethyl alcohol complex.

  Of these, cobalt octylate, cobalt naphthenate, cobalt versatate, bisacetylacetonate and trisacetylacetonate of cobalt are preferred.

  Examples of the organic aluminum include trialkylaluminums such as trimethylaluminum, triethylaluminum, triisobutylaluminum, trihexylaluminum, trioctylaluminum, tridecylaluminum, dimethylaluminum chloride, dimethylaluminum bromide, diethylaluminum chloride, diethylaluminum bromide, and diethylaluminum Dialkylaluminum halides such as iodide, dibutylaluminum chloride, dibutylaluminum bromide, and dibutylaluminum iodide; and alkyl chlorides such as methylaluminum sesquichloride, methylaluminum sesquibromide, ethylaluminum sesquichloride, and ethylaluminum sesquibromide Kiharogen aluminum, methyl aluminum dichloride, methyl aluminum dibromide, ethyl aluminum dichloride, ethyl aluminum dibromide, butyl aluminum dichloride, monoalkyl aluminum halide such as butyl aluminum dibromide and the like. These may be used alone, or a plurality of them may be selected and mixed. Among them, diethyl aluminum chloride is preferably used.

In the transition metal catalyst of the present invention, the amount of the cobalt compound to be added may be in any range depending on the desired degree of branching, but is preferably 1 × 10 ⁻⁷ to 1 × 10 ⁷ per 1 mol of polybutadiene. ^-3 mol, particularly preferably 5 × 10 ^-7 to 1 × 10 ^-4 mol.

Depending on the desired degree of branching, the amount of organoaluminum can be in any range, but is preferably 1 × 10 ^{−5 to} 5 × 10 ⁻² mol per 1 mol of polybutadiene, particularly preferably 1 mol of organoaluminum. It is from 5 × 10 ⁻⁵ to 1 × 10 ⁻² mol.

  The amount of water added in the branching reaction can be in any range depending on the desired degree of branching, but is preferably 1.5 mol or less, and particularly preferably 1 mol or less, per 1 mol of the organoaluminum compound. .

  After performing polymerization for a predetermined time, after terminating the polymerization by injecting a terminating agent such as alcohol, the inside of the polymerization tank is released as necessary, and post-treatments such as washing and drying steps are performed.

Beam at 100 ° C. toluene solution viscosity of the resulting modified polybutadiene (T-cp) in the present invention - D - viscosity (ML _{1 + 4)} ratio _{(T-cp / ML 1 +} 4) is 0.5 to 3 .5, preferably 1.5-3, more preferably 2-3.

The modified polybutadiene obtained in the present invention has a toluene solution viscosity (Tcp) of preferably 30 to 300, and more preferably 100 to 200.

  The modified polybutadiene obtained by the present invention has a cold flow rate (CF) of less than 20, preferably less than 15.

The modified polybutadiene obtained in the present invention has a Mooney viscosity (ML _{1 + 4} ) at 100 ° C. of preferably 10 to 200, particularly preferably 25 to 100.

  The modified polybutadiene obtained in the present invention preferably has a cis-1,4 structure of 65 to 95% and a vinyl structure of 30 to 4%.

  The modified polybutadiene obtained in the present invention preferably has an intrinsic viscosity of 0.5 to 7.0 in toluene at 30 ° C.

  In 100 parts by weight of the impact-resistant styrenic resin composition of the present invention, a rubbery polymer 1 to 25, preferably 5 to 5, obtained by modifying the above high cis-high vinyl polybutadiene in the presence of a transition metal catalyst. -20 parts by weight. When the amount is less than the above range, the effect of the present invention is not obtained, and the impact resistance of the resin is improved with an increase in the content of the rubber-like polymer. The control of the rubber particle diameter becomes difficult, and the effect of the present invention cannot be exhibited, and the industrial utility value is lost.

  As a method for producing the rubber-modified impact-resistant polystyrene-based resin composition of the present invention, a method in which a styrene-based monomer is polymerized in the presence of a rubber-like polymer is employed, and a bulk polymerization method or a bulk suspension polymerization method is economical. This is an advantageous method. Styrene-based monomers such as alkyl-substituted styrenes such as styrene, α-methylstyrene and p-methylstyrene, and halogen-substituted styrenes such as chlorostyrene are known for producing rubber-modified impact-resistant polystyrene resin compositions. Or a mixture of two or more of the styrene-based monomers described above. Of these, styrene is preferred.

  If necessary, in addition to the above rubber-like polymer, a styrene-butadiene copolymer, ethylene-propylene, ethylene-vinyl acetate, acrylic rubber or the like may be used in combination with the above-mentioned rubber-like polymer within 50% by weight of the above-mentioned rubber-like polymer. it can. Further, resins produced by these methods may be blended. Further, a polystyrene resin not containing the rubber-modified polystyrene resin composition produced by these methods may be mixed and produced. As an example of the above bulk polymerization method, a rubber-like polymer (1 to 25% by weight) is dissolved in a styrene monomer (99 to 75% by weight), and in some cases, a solvent, a molecular weight regulator and a polymerization initiator are dissolved. Is added to convert the rubbery polymer to particles having a styrene monomer conversion of 10 to 40%. Until these rubber particles are generated, the rubber phase forms a continuous phase. Further, the polymerization is continued, and the rubber-modified impact-resistant polystyrene resin composition is produced by polymerizing to a conversion of 50 to 99% through a phase conversion (particle forming step) into a dispersed phase as rubber particles.

  The dispersion particles (rubber particles) of the rubber-like polymer referred to in the present invention are particles dispersed in a resin and are composed of a rubber-like polymer and a polystyrene-based resin. Occluded without binding. The dispersion particles of the rubbery polymer referred to in the present invention having a diameter in the range of 0.5 to 7.0 μm, preferably in the range of 1.0 to 3.0 μm can be suitably produced.

In the present invention, a graft ratio of 150 to 350 can be suitably produced.
The method may be a batch method or a continuous production method, and is not particularly limited.

  In the present invention, the raw material solution mainly composed of the styrene-based monomer and the rubber-like polymer is polymerized in a complete mixing type reactor, but as the complete mixing type reactor, the raw material solution is uniformly mixed in the reactor. Is preferable as long as the stirring blade is maintained, and a preferable example is a stirring blade of a type such as a helical ribbon, a double helical ribbon, and an anchor. It is preferable to attach a draft tube to the helical ribbon type stirring blade to further enhance the vertical circulation in the reactor.

  In the rubber-modified impact-resistant polystyrene resin composition of the present invention, a stabilizer such as an antioxidant and an ultraviolet absorber, a mold release agent, a lubricant, a coloring agent, and various fillers may be used as needed during or after production. Known additives such as various plasticizers, higher fatty acids, organic polysiloxanes, silicone oils, flame retardants, antistatic agents and foaming agents may be added. The rubber-modified impact-resistant polystyrene resin composition of the present invention can be used for various known molded products, but is used in electric and industrial fields because of its excellent flame retardancy, impact resistance, and tensile strength. Suitable for injection molding.

  For example, it can be used for a wide range of applications such as films and sheets used for home appliances, industrial use, packaging materials, food containers, etc. for housings of color televisions, boomboxes, word processors, typewriters, facsimiles, VTR cassettes, telephones, etc. it can. Also, the high cis-high vinyl polybutadiene can be used for automobile tires and non-tire applications such as golf balls and shoe soles.

Micro molecular extinction coefficient of 967 cm ^-1; by infrared absorption spectrum analysis, cis-1,4 obtained from Hampton method structure; 740 cm ^-1, vinyl structure; 911 cm ^-1, trans-1,4 structure: microstructure The structure was calculated.

  The Mooney (ML) viscosity was measured according to a measurement method specified in JIS-K-6300.

Intrinsic viscosity ([η]) was measured at 30 ° C. using a toluene solution of the polymer.

  Toluene solution viscosity (T-cp) was determined by dissolving 2.28 g of a polymer in 50 ml of toluene, and using a standard solution for calibration of a viscometer (JIS Z8809) as a standard solution. It was measured at 25 ° C. using a 400.

Rubber particle diameter: A rubber-modified impact-resistant polystyrene resin composition is dissolved in dimethylformamide, only the polystyrene portion forming a matrix in the resin is dissolved, and a part of the solution is used as a Coulter counter device manufactured by Nikkaki Co., Ltd. It was dispersed in an electrolytic solution composed of a solvent dimethylformamide and a dispersant ammonium thiocyanate using TA-2 type, and the obtained volume average particle diameter was defined as a rubber particle diameter.

  A graft rate: 1 g of a rubber-modified impact-resistant polystyrene resin is added to 50 ml of a mixed solution of methyl ethyl ketone / acetone = 1/1 (weight ratio), and the mixture is vigorously stirred for 1 hour to dissolve and swell. Next, after insoluble matter is sedimented by a centrifuge, the supernatant is discarded by decantation. The thus obtained methyl ethyl ketone / acetone insoluble matter was dried under reduced pressure at 50 ° C., cooled in a desiccator, and weighed to obtain methyl ethyl ketone / acetone insoluble matter (MEK / AC-insol.g). The graft ratio was calculated from the rubbery polymer content (Rg) calculated from the rubbery polymer content. Graft rate = [MEK / AC-insol. (G) −R (g)] × 100 / R (g)

  Swelling degree: 1 g of a rubber-modified impact-resistant polystyrene resin is dissolved and swelled in 50 ml of toluene with vigorous stirring for 1 hour. Next, after insoluble matter is sedimented by a centrifuge, the supernatant is discarded by decantation. After measuring the weight of the sedimented portion (swollen, undried weight), it was dried in vacuum at 100 ° C., cooled in a desiccator, weighed, and indicated by the weight ratio at the time of swelling / drying.

  Izod impact strength: measured according to JIS K7110 (with notch).

  Dupont impact strength: It was shown as a 50% breaking energy by a Dupont type falling weight tester.

Tensile properties: Yield point strength, break point strength and elongation were measured according to JIS K7113.

Gloss: Gloss was measured according to JIS Z8742 (incident angle 60 °).
Cold flow rate (CF): The obtained rubbery polymer was kept at 50 ° C., sucked in a glass tube having an inner diameter of 6.4 mm with a differential pressure of 180 mmHg for 10 minutes, and the weight of the sucked polymer was measured to determine the weight per minute. The amount of polymer sucked was determined as a measure of the magnitude of cold flow.

(Reference Example 1) (Production of denatured product)
The inside of a 1.7 L autoclave is replaced with nitrogen, 260 ml of cyclohexane and 140 ml of butadiene are charged and stirred. Then, 5 μl of water was added and stirring was continued for 30 minutes. At 110 ° C., 110 ml of hydrogen was measured and injected at 20 ° C. and 1 atm with a cumulative mass flow meter. Then, 0.36 ml of a 1 mol / L toluene solution of triethylaluminum (TEA) was added, and the mixture was stirred for 3 minutes. 0.5 ml of a toluene solution of 5 mmol / L of enilvanadium trichloride (CpVCl ₃ ) and a toluene solution 1 of 2.5 mmol / L of triphenylcarbenium tetrakis (pentafluorophenyl) borate (Ph ₃ CB (C ₆ F ₅ ) ₄ ) The mixture was added in the order of 0.5 ml, and polymerization was performed at a polymerization temperature of 40 ° C. for 30 minutes. Further, 4.8 ml of toluene containing 300 mg / L of water, 0.1 ml of a toluene solution of 1 mol / L of diethyl aluminum chloride (DEAC), and 0.5 ml of a toluene solution of 5 mmol / L of cobalt octylate (Co (Oct) ₂ ) were added. At 40 ° C. for 30 minutes.
After the reaction, ethanol containing 2,6-di-t-butyl-p-cresol was injected to stop the reaction, and then the solvent was evaporated and dried. Table 1 shows the polymerization results.

  (Reference Example 2) Polymers shown in Table 1 were obtained in the same manner as in Reference Example 1 by changing the conditions.

(Reference Example 3) (Production of unmodified product)
The inside of a 1.7 L autoclave is replaced with nitrogen, 260 ml of cyclohexane and 140 ml of butadiene are charged and stirred. Then, 5 μl of water was added and stirring was continued for 30 minutes. At 110 ° C., 110 ml of hydrogen was measured and injected at 20 ° C. and 1 atm with a cumulative mass flow meter. Then, 0.36 ml of a 1 mol / L toluene solution of triethylaluminum (TEA) was added, and the mixture was stirred for 3 minutes. 0.5 ml of a toluene solution of 5 mmol / L of enilvanadium trichloride (CpVCl ₃ ) and a toluene solution 1 of 2.5 mmol / L of triphenylcarbenium tetrakis (pentafluorophenyl) borate (Ph ₃ CB (C ₆ F ₅ ) ₄ ) The mixture was added in the order of 0.5 ml, and polymerization was performed at a polymerization temperature of 40 ° C. for 30 minutes.
After the reaction, ethanol containing 2,6-di-t-butyl-p-cresol was injected to stop the reaction, and then the solvent was evaporated and dried. Table 1 shows the polymerization results.

  (Reference Example 4) Polymers shown in Table 1 were obtained in the same manner as in Reference Example 3 by changing the conditions.

(Reference Examples 5 to 6) Using an existing catalyst system (such as a cobalt compound or a lithium compound), it was produced under ordinary polymerization conditions. Table 1 shows the results.

[Example 1]
A 1.5-liter autoclave equipped with a stirrer was replaced with nitrogen gas, and 465 g of styrene and 35 g (7 parts by weight of rubber) of HCHVBR produced in Reference Examples shown in Table 1 were added and dissolved. Then, 0.15 g of n-dodecyl mercaptan was added, and the mixture was prepolymerized at 135 ° C. for 1 hour and a half with stirring under the conditions shown in Table 4 until the conversion of styrene became 30%. Next, 500 ml of a 0.5 wt% polyvinyl alcohol aqueous solution was injected into the prepolymerized solution, and 1.0 g (0.2 part by weight) of benzoyl peroxide and 1.0 g (0.2 part by weight) of dicumyl peroxide were added. In addition, polymerization was continuously carried out with stirring at 100 ° C. for 2 hours, at 125 ° C. for 3 hours, and at 140 ° C. for 2 hours. After cooling to room temperature, the polymer in the form of beads was filtered from the polymerization reaction mixture, washed with water and dried. This was pelletized by an extruder to obtain 450 g of an impact-resistant styrene resin. Each of the obtained rubber-modified impact-resistant styrene resin compositions was injection-molded to prepare a test piece for measuring physical properties, and the physical properties were measured. The results are shown in Table 2.

(Examples 2 to 12) (Comparative Examples 1 to 9)
Table 2 shows the results of the obtained rubber-modified impact-resistant styrenic resin composition under different conditions.

Claims (6)

In a rubber-modified impact-resistant styrenic resin composition containing a rubbery polymer,
The rubbery polymer is a high cis-high vinyl polybutadiene, a modified polybutadiene obtained by modification in the presence of a transition metal catalyst, and a 5% toluene solution viscosity (T-cp) measured at 30 ° C. and 100 ° C. Modified polybutadiene having a ratio (T-cp / ML _{1 + 4} ) to the Mooney viscosity (ML _{1 + 4} ) in the range of 0.5 to 3.5 and a cold flow rate (CF) of less than 20 mg / min. A rubber-modified impact-resistant styrenic resin composition characterized by using: The rubber-modified impact-resistant styrene resin composition according to claim 1, wherein the unmodified high cis-high vinyl polybutadiene is produced by a metallocene catalyst. The rubber-modified impact-resistant styrene resin composition according to claim 1, wherein the modified polybutadiene has a cis-1,4 structure of 65 to 95% and a vinyl structure of 30 to 4%. The rubber-modified impact-resistant styrenic resin composition according to any one of claims 1 to 3, wherein the modified polybutadiene has an intrinsic viscosity measured at 30 ° C in toluene of 0.5 to 7.0. The metallocene catalyst is a catalyst comprising (A) a metallocene complex of a transition metal compound, and (B) an ionic compound of a non-coordinating anion and a cation and / or an alumoxane. The rubber-modified impact-resistant styrenic resin composition according to 1. The rubber-modified impact-resistant styrene according to any one of claims 1 to 5, comprising 1 to 25% by weight of the rubbery polymer and 99 to 75% by weight of the styrene resin composition.