WO1996024633A1 - Rubber-modified styrenic resin composition - Google Patents
Rubber-modified styrenic resin composition Download PDFInfo
- Publication number
- WO1996024633A1 WO1996024633A1 PCT/JP1996/000258 JP9600258W WO9624633A1 WO 1996024633 A1 WO1996024633 A1 WO 1996024633A1 JP 9600258 W JP9600258 W JP 9600258W WO 9624633 A1 WO9624633 A1 WO 9624633A1
- Authority
- WO
- WIPO (PCT)
- Prior art keywords
- rubber
- weight
- polymer
- styrene
- resin composition
- Prior art date
- Legal status (The legal status is an assumption and is not a legal conclusion. Google has not performed a legal analysis and makes no representation as to the accuracy of the status listed.)
- Ceased
Links
Classifications
-
- C—CHEMISTRY; METALLURGY
- C08—ORGANIC MACROMOLECULAR COMPOUNDS; THEIR PREPARATION OR CHEMICAL WORKING-UP; COMPOSITIONS BASED THEREON
- C08L—COMPOSITIONS OF MACROMOLECULAR COMPOUNDS
- C08L51/00—Compositions of graft polymers in which the grafted component is obtained by reactions only involving carbon-to-carbon unsaturated bonds; Compositions of derivatives of such polymers
- C08L51/04—Compositions of graft polymers in which the grafted component is obtained by reactions only involving carbon-to-carbon unsaturated bonds; Compositions of derivatives of such polymers grafted on to rubbers
-
- C—CHEMISTRY; METALLURGY
- C08—ORGANIC MACROMOLECULAR COMPOUNDS; THEIR PREPARATION OR CHEMICAL WORKING-UP; COMPOSITIONS BASED THEREON
- C08F—MACROMOLECULAR COMPOUNDS OBTAINED BY REACTIONS ONLY INVOLVING CARBON-TO-CARBON UNSATURATED BONDS
- C08F279/00—Macromolecular compounds obtained by polymerising monomers on to polymers of monomers having two or more carbon-to-carbon double bonds as defined in group C08F36/00
-
- C—CHEMISTRY; METALLURGY
- C08—ORGANIC MACROMOLECULAR COMPOUNDS; THEIR PREPARATION OR CHEMICAL WORKING-UP; COMPOSITIONS BASED THEREON
- C08F—MACROMOLECULAR COMPOUNDS OBTAINED BY REACTIONS ONLY INVOLVING CARBON-TO-CARBON UNSATURATED BONDS
- C08F279/00—Macromolecular compounds obtained by polymerising monomers on to polymers of monomers having two or more carbon-to-carbon double bonds as defined in group C08F36/00
- C08F279/02—Macromolecular compounds obtained by polymerising monomers on to polymers of monomers having two or more carbon-to-carbon double bonds as defined in group C08F36/00 on to polymers of conjugated dienes
Definitions
- the present invention relates to a rubber-modified styrenic resin composition having excellent mechanical strength and gloss and excellent coloring properties.
- HIPS rubber-modified styrenic resin
- An object of the present invention is to provide a rubber-modified styrenic resin composition which overcomes the above drawbacks and has excellent coloring properties without lowering the balance between gloss and mechanical strength.
- the present invention comprises a styrene polymer obtained by dissolving a rubber-like polymer in a styrene-based monomer and performing a graft polymerization, and the rubber-like polymer is composed of 80 to 96% by weight and a rubber-like polymer of 20 to 4% by weight.
- a rubber-modified styrenic resin composition obtained by dissolving a rubber-like polymer in a styrene-based monomer and performing a graft polymerization, and the rubber-like polymer is composed of 80 to 96% by weight and a rubber-like polymer of 20 to 4% by weight.
- the rubbery polymer is dispersed in the styrene polymer matrix as particles having a volume average particle diameter in the range of 0.5 to 1.6 / m, and
- a part of the styrene-based polymer has a number average particle size of 0.13111 or more to 0.20 m and a particle size distribution of 1.1. It has a salami structure that is dispersed and contained within the range of 5 to 1.35.
- the dispersed particles of the rubber-like polymer relate to a rubber-modified styrenic resin composition characterized in that the swelling ratio in toluene is in the range of 7 to 12.
- the styrenic monomer forming the rubber-modified styrenic polymer composition of the present invention means not only a styrenic monomer alone but also a combination with another vinylic monomer copolymerizable with the styrenic monomer.
- the styrene monomer include aromatic monovinyl compounds such as styrene, -methylstyrene, 0-methylstyrene, m-methylstyrene, p-methylstyrene, vinylethylbenzene, vinylxylene, and vinylnaphthalene. it can.
- vinyl monomer copolymerizable with the styrene monomer examples include, for example, methyl methacrylate, ethyl methacrylate, methyl acrylate, ethyl acrylate, acrylonitrile, methacrylonitrile, and methacrylic acid. , Acrylic acid, maleic anhydride, phenyl maleimide, or a halogen-containing vinyl monomer. These monomers may be used alone or in combination of two or more. It can be used in an amount of usually 30% by weight or less, preferably 10% by weight or less, based on all styrene-based monomers containing styrene.
- the proportion of the graft polymerized rubbery polymer is 4 to 20% by weight based on 96 to 80% by weight of the styrene polymer matrix. If the amount of the rubber-like polymer is less than 4% by weight, the impact resistance is insufficient. If the amount exceeds 20% by weight, the rigidity is reduced to a practical range or less, which is not preferable.
- the volume average particle diameter of the rubbery polymer dispersed by graft polymerization in the styrenic polymer matrix is 0.5 to 1.6 ⁇ m. m, preferably 0.8-1.31m. If the average particle size is less than 0.5 / m, the impact resistance is insufficient, and if it exceeds 1.6 zm, the gloss is significantly reduced.
- the number average particle diameter of the styrene-based polymer dispersed and contained in the dispersed rubber-like polymer particles is 0.13 or more to 0.20 m. Needs to be 0.14 to 0.19 / m, more preferably 0.15 to 0.18 / m. If the number average particle diameter of the styrene polymer contained in the dispersion is 0.13 m or less, the mechanical strength tends to decrease sharply, and if it exceeds 0.20 / m, the coloring property is significantly reduced.
- the particle size distribution of the styrene-based polymer dispersed and contained in the dispersed rubber-like polymer particles it is necessary to adjust the particle size distribution of the styrene-based polymer dispersed and contained in the dispersed rubber-like polymer particles to 1.15 to 1.5. It is important to control in the range of 1.35, preferably 1.20 to 1.30.
- the particle size distribution is 1.15 or less, the mechanical strength, particularly the falling weight impact strength is reduced, and when the particle size distribution is 1.35 or more, the coloring property is deteriorated.
- Making the particle size of the styrene-based polymer contained in the dispersion fine and uniform is effective for improving the coloring property.
- making the particle size finer and more than necessary is mechanical. The strength, especially the tensile elongation and the falling weight impact strength are reduced, and it becomes difficult to maintain the balance of physical properties, so that the object of the present invention cannot be achieved.
- the swelling ratio of the dispersed rubber-like polymer particles in toluene is in the range of 7 to 12, preferably 8 to 11.
- the rubber-like polymer used in the present invention preferably has a solution viscosity (SV value) of a 5% by weight styrene solution at 25 ° C. of 10 to LOO cps, and more preferably 20 to 90 cps. .
- the solution viscosity (SV value) is less than 10 cps, the rubber particle diameter tends to be too small, and the mechanical strength is unfavorably reduced. If the solution viscosity is more than 100 cps, the rubber particle size tends to be too large. It is not preferable because gloss decreases.
- the rubbery polymer to be used is not particularly limited as long as it satisfies the above conditions.Polybutadiene, styrene-butadiene copolymer, polyisoprene, butadiene-styrene-polyisoprene copolymer, natural rubber, etc. Can be used.
- the microstructure of the polybutadiene portion may be low-cis polybutadiene rubber, high-cis polybutadiene rubber, or a mixture of low-cis polybutadiene rubber and high-cis polybutadiene rubber. Is also good.
- the structure of the styrene-butadiene copolymer may be a random type, a block type or a tapered type. One of these rubbery polymers can be used alone, or two or more can be used in combination.
- the balance between the coloring property and the gloss is further improved, so that the styrene-butadiene copolymer is preferably contained as the rubbery polymer.
- the amount is preferably at least 50% by weight, more preferably at least 75% by weight.
- the styrene content in the styrene-butadiene copolymer is preferably from 1 to 2 0% by weight, more preferably 1 to 10% by weight is desirable.
- the rubber-modified styrenic resin composition of the present invention may contain various additives as needed, for example, an internal lubricant, a plasticizer, an antioxidant, an ultraviolet absorber, an antistatic agent, a release agent, a flame retardant, Additives such as dyes and pigments and silicon oil can also be blended. These additives can be added at any stage. For example, it may be added at the stage of molding a molded article, or may be added at the stage of polymerization of a product.
- a rubber-like polymer is It can be obtained by dissolving in a ren-based monomer and performing graft polymerization by bulk polymerization or solution polymerization.
- a particularly preferred polymerization method of the present invention is to prepare a raw material solution by mixing and dissolving a rubber-like polymer in advance with a specific amount of polystyrene in a styrene-based monomer, and performing a bulk polymerization method or a solution polymerization method. .
- the raw material solution is preheated to about 70 to 120 ° C in advance and then continuously charged into a Bragg-type one-type reactor such as a tower type or static mixer type to perform bulk polymerization or solution polymerization. It is desirable to overlap.
- a Bragg-type one-type reactor such as a tower type or static mixer type to perform bulk polymerization or solution polymerization. It is desirable to overlap.
- the larger the polystyrene content in the raw material mixed solution at the time of such graft polymerization the smaller the particle size of the styrene-based polymer dispersed and included in the produced rubbery polymer-dispersed particles tends to be.
- the particle size control of the styrene-based polymer dispersed and incorporated in the rubber-like polymer-dispersed particles specified in the present invention is performed by adjusting the amount of the polystyrene and the amount of the rubber-like polymer in the mixed solution. be able to.
- the amount of polystyrene to be mixed in the raw material mixed solution should be in the range of 2 to 30% by weight, and the relationship between the rubbery polymer content R (% by weight) and the polystyrene content P (% by weight) Satisfies 0.2 and PZR 3 and, in the preheating stage, adjusts to the state before the rubber phase inversion, and then feeds it into the plug flow reactor, where it is stirred under no mixing conditions. Rubber phase. It is preferable to proceed the graft polymerization reaction while inverting. By such adjustment, it is possible to easily control the particle size of the rubber-like polymer dispersed particles specified in the present invention, the particle size of the styrene-based polymer dispersed in the dispersion particles, and the like.
- a solvent can be added as needed to adjust the viscosity in the system accompanying the dissolution of polystyrene.
- an organic solvent selected from aromatic hydrocarbons such as toluene, xylene, and ethylbenzene, and ketones such as methylethylketone is preferably 30 parts by weight or less based on 100 parts by weight of the raw material mixed solution. Is blended in a proportion of 10 to 20 parts by weight.
- an organic peroxide as a polymerization initiator, a chain transfer agent, an antioxidant, a mineral oil, and the like can be appropriately added.
- the polymerization reaction was continued until the polymerization conversion of the styrene monomer in the raw material solution reached 60 to 98% by weight, and then devolatilized by a devolatilizer under a negative pressure while performing appropriate heat treatment.
- the desired rubber-modified styrene resin composition can be obtained by removing the unreacted monomers and the solvent by volatilization. Adjustment of the swelling ratio can be usually performed by selecting conditions such as a heat treatment temperature and time after the polymerization is completed and before or after the unpolymerized monomer is removed.
- the properties of the resin were determined by the following methods.
- Resin is stained with osmium oxide and electron micrographs are taken by ultra-thin section method
- the aromatic vinyl-based polymer particles included in the dispersed rubber particles in the photograph magnified 10,000 times, for particles of 0.05 m or more, the area of the particles is determined, and the circle equivalent is calculated. The number average particle diameter and the weight average particle diameter of 500 to 100 particles are shown. The particle size distribution is calculated as weight average particle size / number average particle size.
- the resin lg was dissolved in 30 mL of toluene, the insoluble matter (rubber particles) was sedimented by a centrifuge, the supernatant was discarded, and the sedimented swelling gel was weighed.
- the weight of the dried gel obtained by drying the gel to a constant weight was determined by the following equation.
- the following mixture (a) was continuously supplied as a raw material liquid at a supply speed of 30 torr to a complete mixing tank type preheater having an internal volume of 25 liters.
- SBR Styrene-butadiene rubber
- Ethylbenzene (EB) 10 parts by weight
- the entire reactor was continuously charged to the first reactor of a 45 liter tower type plug flow reactor equipped with a stirrer to carry out polymerization.
- the polymerization temperature in the first reactor was adjusted so that a temperature gradient was generated in the range of 100 to 115 ° C so that the temperature increased along the flow direction.
- the rubbery polymer has not yet undergone phase inversion, and as a result of polymerization while stirring in the first reactor, the polymerization liquid at the outlet of the first reactor is in a state where phase inversion has been completed. there were.
- the entire amount of the above-mentioned polymerization solution was continuously charged into a second reactor having three 50-liter static mixer-type Bragg flow reactors arranged in series, and the polymerization was continued to polymerize styrene.
- the polymerization was allowed to proceed to a rate of 88%, and this polymerization solution was subjected to heat treatment at 230 ° C in a twin-screw extruder equipped with a 3-vent to remove volatile components under reduced pressure and then pelletized.
- Ethylbenzene (EB) 10 parts by weight
- Styrene-butadiene copolymer 2% by weight
- Ethylbenzene (EB) 10 parts by weight
- Ethylbenzene (EB) 10 parts by weight
- Styrene-butadiene rubber 6% by weight
- Ethylbenzene (EB) 10 parts by weight
- Comparative Example 1 the polystyrene particles contained in the rubber particles were excessively fine and uniform, and the coloring property was good, but the mechanical strength, especially the tensile elongation, and the falling weight impact strength was significantly reduced. are doing. Comparative Example 2
- Ethylbenzene (EB) 10 parts by weight
- Ethylbenzene (EB) 10 parts by weight
- Comparative Example 3 the particle size of the polystyrene included in the rubber particles was large and non-uniform, and the coloring property was extremely poor. Comparative Example 4
- Example 1 the experiment was performed under the same conditions as in Example 1 except that the following mixture (h) was used as a raw material liquid and the temperature of the twin-screw extruder was set to 210 ° C. Table 1 shows the physical properties of the obtained resin.
- Ethylbenzene (EB) 10 parts by weight
- the rubber-modified styrenic resin composition obtained by the present invention not only has good mechanical strength but also has excellent gloss and coloring properties and is well-balanced. For this reason, the resin composition according to the present invention is suitable for products used for front panels and housings used in the electric and electronic fields where particularly good appearance characteristics are required.
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- Chemical & Material Sciences (AREA)
- Health & Medical Sciences (AREA)
- Chemical Kinetics & Catalysis (AREA)
- Medicinal Chemistry (AREA)
- Polymers & Plastics (AREA)
- Organic Chemistry (AREA)
- Graft Or Block Polymers (AREA)
- Compositions Of Macromolecular Compounds (AREA)
Description
Claims
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| US08/894,848 US6031050A (en) | 1995-02-08 | 1996-02-07 | Rubber-modified styrenic resin composition |
Applications Claiming Priority (2)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| JP7020186A JPH08208940A (ja) | 1995-02-08 | 1995-02-08 | ゴム変性スチレン系樹脂組成物 |
| JP7/20186 | 1995-02-08 |
Publications (1)
| Publication Number | Publication Date |
|---|---|
| WO1996024633A1 true WO1996024633A1 (en) | 1996-08-15 |
Family
ID=12020155
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| PCT/JP1996/000258 Ceased WO1996024633A1 (en) | 1995-02-08 | 1996-02-07 | Rubber-modified styrenic resin composition |
Country Status (5)
| Country | Link |
|---|---|
| US (1) | US6031050A (ja) |
| JP (1) | JPH08208940A (ja) |
| KR (1) | KR100360003B1 (ja) |
| CN (1) | CN1131881C (ja) |
| WO (1) | WO1996024633A1 (ja) |
Cited By (1)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| US6310148B1 (en) | 1998-07-30 | 2001-10-30 | Dainippon Ink And Chemicals, Ltd. | Stryrene resin composition and process for producing the same |
Families Citing this family (9)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| US5852124A (en) * | 1996-08-06 | 1998-12-22 | Chi Mei Corporation | Rubber-modified styrenic resin composition |
| WO1998012258A1 (en) * | 1996-09-19 | 1998-03-26 | Nippon Steel Chemical Co., Ltd. | Flame-retardant styrenic resin composition |
| JP2002113818A (ja) * | 2000-10-06 | 2002-04-16 | Daicel Chem Ind Ltd | 樹脂シート及び電子部品搬送用成形品 |
| ITMI20031420A1 (it) * | 2003-07-11 | 2005-01-12 | Polimeri Europa Spa | Polimeri vinilaromatici rinforzati con gomma |
| US7129297B2 (en) * | 2003-09-29 | 2006-10-31 | Fina Technology, Inc. | Polystyrene blends and a method of making same |
| JP5242174B2 (ja) * | 2006-01-31 | 2013-07-24 | Psジャパン株式会社 | ゴム変性スチレン系樹脂及びその樹脂を含んでなる光拡散板 |
| US9079982B2 (en) * | 2010-10-29 | 2015-07-14 | Fina Technology, Inc. | Methods of making high impact polystyrene |
| WO2016195601A1 (en) * | 2015-06-04 | 2016-12-08 | Irpc Public Company Limited | Polymer compositions and processes for producing the same |
| KR102374187B1 (ko) * | 2019-12-24 | 2022-03-14 | 한화토탈 주식회사 | 고무 조성물의 제조방법, 이의 방법으로 제조된 고무 조성물 및 이를 이용하여 제조된 타이어 |
Citations (2)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| JPS60233116A (ja) * | 1984-05-04 | 1985-11-19 | Asahi Chem Ind Co Ltd | ゴム補強芳香族モノビニル樹脂組成物 |
| JPS60233118A (ja) * | 1984-05-04 | 1985-11-19 | Asahi Chem Ind Co Ltd | ゴム変性芳香族モノビニル樹脂組成物 |
Family Cites Families (5)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| DE3002394A1 (de) * | 1980-01-24 | 1981-07-30 | Röhm GmbH, 6100 Darmstadt | Verfahren zur herstellung schlagzaeher formmassen |
| JPS59221318A (ja) * | 1983-06-01 | 1984-12-12 | Asahi Chem Ind Co Ltd | ゴム変性芳香族モノビニル樹脂組成物 |
| JPS60130614A (ja) * | 1983-12-16 | 1985-07-12 | Asahi Chem Ind Co Ltd | ゴム変性芳香族モノビニル重合体樹脂組成物 |
| JPS60130613A (ja) * | 1983-12-16 | 1985-07-12 | Asahi Chem Ind Co Ltd | ゴム変性された芳香族モノビニル重合体樹脂組成物 |
| JPS6333461A (ja) * | 1986-07-28 | 1988-02-13 | Asahi Chem Ind Co Ltd | 高光沢ゴム補強ポリスチレン組成物 |
-
1995
- 1995-02-08 JP JP7020186A patent/JPH08208940A/ja active Pending
-
1996
- 1996-02-07 CN CN96191865A patent/CN1131881C/zh not_active Expired - Fee Related
- 1996-02-07 US US08/894,848 patent/US6031050A/en not_active Expired - Lifetime
- 1996-02-07 KR KR1019970705435A patent/KR100360003B1/ko not_active Expired - Fee Related
- 1996-02-07 WO PCT/JP1996/000258 patent/WO1996024633A1/ja not_active Ceased
Patent Citations (2)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| JPS60233116A (ja) * | 1984-05-04 | 1985-11-19 | Asahi Chem Ind Co Ltd | ゴム補強芳香族モノビニル樹脂組成物 |
| JPS60233118A (ja) * | 1984-05-04 | 1985-11-19 | Asahi Chem Ind Co Ltd | ゴム変性芳香族モノビニル樹脂組成物 |
Cited By (2)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| US6310148B1 (en) | 1998-07-30 | 2001-10-30 | Dainippon Ink And Chemicals, Ltd. | Stryrene resin composition and process for producing the same |
| EP1026183A4 (en) * | 1998-07-30 | 2003-04-02 | Dainippon Ink & Chemicals | STYROLHARS COMPOSITION AND METHOD FOR THE PRODUCTION THEREOF |
Also Published As
| Publication number | Publication date |
|---|---|
| JPH08208940A (ja) | 1996-08-13 |
| CN1173887A (zh) | 1998-02-18 |
| KR19980702040A (ko) | 1998-07-15 |
| CN1131881C (zh) | 2003-12-24 |
| US6031050A (en) | 2000-02-29 |
| KR100360003B1 (ko) | 2003-04-10 |
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