JP2014205797A - Styrenic oriented sheet and molded product of the same - Google Patents

Abstract

PROBLEM TO BE SOLVED: To provide a molded product by using together an impact-resistant styrenic resin, a polylactic acid, and a polyphenylene ether resin without damaging usefulness of each, and especially to provide a styrenic oriented film and a molded product of the same, which intended to satisfy both strength of a molded product, oil resistance, and working characteristics.SOLUTION: Provided is a styrenic oriented sheet obtained by biaxially drawing a styrenic resin composition comprising an impact-resistant styrenic resin (A), polylactic acid (B), and a polyphenylene ether resin (C); and a molded product obtained by molding the same.

Description

  The present invention relates to a sheet formed by stretching a resin composition containing an impact-resistant styrene-based resin, polylactic acid, and polyphenylene ether-based resin, and a molded article formed by molding the sheet.

  In recent years, it has been recognized by general consumers that the use of plastic products containing various biodegradable polymers is preferable from the viewpoint of environmental protection and the use of plant-derived materials from the viewpoint of saving petroleum resources. Attempts to use biodegradable polymers and plant-derived polymers as raw materials have been widely conducted for industrial products.

  In particular, polylactic acid is a plant-derived and biodegradable polymer, and among the biodegradable polymers, it is practically superior because it has a relatively high melting point, toughness, transparency, and chemical resistance. Recognized as a polymer.

  On the other hand, the styrene resin is excellent in moldability and practical physical properties such as rigidity. Therefore, studies have been made to make use of the characteristics of these resins. For example, studies have been made on blending a styrene resin and polylactic acid to ensure fluidity and improve mechanical properties. (For example, refer to Patent Document 1). However, the compatibility between styrene-based resins and polylactic acid is very poor, and it is difficult to design products that take advantage of the physical properties required by the market and the characteristics of each resin by simply blending and melting and mixing. In addition, by using a ternary system of styrene resin, polylactic acid and polyphenylene ether resin, improvement of processing characteristics (fluidity) is being studied while suppressing deterioration of mechanical properties. (For example, refer to Patent Document 2) However, as in the above-described reason, it is a fact that a product design that fully utilizes the characteristics of each resin cannot be achieved by simply blending and melt-mixing.

JP 2008-050426 A JP 2009-22214 A

  In view of the above circumstances, the problem to be solved by the present invention is to obtain a molded article using these in combination without impairing the usefulness of each of impact-resistant styrene resin, polylactic acid and polyphenylene ether resin. In particular, it is an object of the present invention to provide a styrene-based stretched sheet and a molded product thereof that are compatible with the strength, oil resistance, and processing characteristics of the molded product.

  As a result of intensive studies to solve the above problems, the present inventors have obtained a sheet obtained by stretching a resin composition containing an impact-resistant styrene resin, polylactic acid, and polyphenylene ether resin in a biaxial direction. However, the present inventors have found that it is possible to provide a molded product having practical physical properties and excellent in moldability and oil resistance, and completed the present invention.

  That is, the present invention provides a styrene-based stretched sheet characterized by biaxially stretching a styrene-based resin composition containing an impact-resistant styrene-based resin, polylactic acid, and polyphenylene ether-based resin, and molding the same. To provide a molded product.

  The styrene-based stretched sheet of the present invention is excellent in processability, and the resulting molded product has good mechanical strength and oil resistance. Moreover, it can reduce an environmental load by mix | blending a plant-derived resin, and can also be used for various general purpose molded objects, and is preferable from a viewpoint of environmental protection.

The present invention is described in detail below.
The impact-resistant styrene resin of the component (A) used in the present invention may be a polystyrene resin containing a component such as rubber. For example, a rubber-like polymer in a continuous phase composed of a polymer of styrene alone. As the resin obtained by graft polymerization and particle dispersion, those generally available can be used. Examples of the rubber component contained in the impact-resistant styrene resin include polybutadiene, styrene-butadiene copolymer, polyisoprene, and butadiene-isoprene copolymer. In particular, it is preferably contained as a polybutadiene or styrene-butadiene copolymer.

  The fluidity of the impact-resistant styrenic resin (A) used in the present invention is 1 to 10 g / 10 min. From the viewpoint of processing characteristics during stretch molding and thickness uniformity during secondary molding. It is preferable that it exists in the range.

  Further, the content of the rubber component in the impact-resistant styrene resin (A) is preferably 2.0 to 15.0% by mass from the viewpoint of coexistence of impact strength and processing characteristics at the time of stretch molding. .

  The polylactic acid (B) used in the present invention is obtained by, for example, saccharifying starch obtained from corn, potatoes, etc., further obtaining lactic acid by lactic acid bacteria, and then cyclizing the lactic acid to form lactide. Generally available polylactic acid (B) obtained by ring polymerization can be used. Also, polylactic acid obtained by synthesizing lactide from petroleum and ring-opening polymerization thereof, or polylactic acid obtained by obtaining lactic acid from petroleum and directly dehydrating and condensing it may be used.

  The lactic acid constituting the polylactic acid can be used by mixing L-lactic acid and D-lactic acid. However, either one of L-lactic acid or D-lactic acid is preferred because the stretched sheet obtained has excellent heat resistance. It is preferable that it is what consists of an isomer of this, and, specifically, the thing with a D-isomer content rate (ratio of D-lactic acid with respect to the total mass of lactic acid used as a raw material) is 3.0% or less.

  Furthermore, other components may be copolymerized with polylactic acid (B) in addition to D-lactic acid and L-lactic acid, which are main constituent monomers. Examples of other copolymer components include ethylene glycol, propylene glycol, butanediol, oxalic acid, adipic acid, and sebacic acid. Such a copolymer component is preferably contained in an amount of generally 0 to 30 mol%, more preferably 0 to 10 mol%, in all monomer components.

  The molecular weight and molecular weight distribution of polylactic acid (B) are not particularly limited as long as it can be substantially molded, but the weight average molecular weight is preferably 10,000 to 400,000, more preferably 40,000 to 200,000. It is a range.

  The polyphenylene ether resin (C) used in the present invention is a homopolymer or copolymer composed of a repeating unit represented by the following general formula (1). It may be a mixture of two or more different resins.

［式（１）中、Ｒ_１、Ｒ_２、Ｒ_３、Ｒ_４はそれぞれ独立して、水素原子、ハロゲン原子、置換基を有していても良いアルキル基、アルコキシ基又は置換基を有していても良いアリール基であり、ｎは繰り返し数である。］

[In Formula (1), R ₁ , R ₂ , R ₃ and R ₄ each independently have a hydrogen atom, a halogen atom, an alkyl group, an alkoxy group or a substituent which may have a substituent. And n is the number of repetitions. ]

  Examples of the homopolymer represented by the general formula (1) include poly (2,6-dimethyl-1,4-phenylene) ether and poly (2-methyl-6-ethyl-1,4-phenylene). Ether, poly (2,6-diethyl-1,4-phenylene) ether, poly (2-ethyl-6-n-propyl-1,4-phenylene) ether, poly (2,6-di-n-propyl-) 1,4-phenylene) ether, poly (2-methyl-6-n-butyl-1,4-phenylene) ether, poly (2-ethyl-6-isopropyl-1,4-phenylene) ether, poly (2- Methyl-6-chloroethyl-1,4-phenylene) ether, poly (2-methyl-6-hydroxyethyl-1,4-phenylene) ether, poly (2,6-dichloro-1,4-phenylene) ether Etc. The.

  Examples of the copolymer include a copolymer of 2,6-dimethylphenol and 2,3,6-trimethylphenol, a copolymer of 2,6-dimethylphenol and o-cresol, -A copolymer of dimethylphenol and 2,3,6-trimethylphenol and the like.

  Among these, particularly preferred polyphenylene ether resins (C) are poly (2,6-dimethyl-1,4-phenylene) ether, co-polymerization of 2,6-dimethylphenol and 2,3,6-trimethylphenol. It is a coalescence or a mixture thereof.

  The method for producing the polyphenylene ether-based resin (C) used in the present invention is not particularly limited, and can be obtained by various methods. For example, US Pat. Nos. 3,306,874 and 3,306,875 , 3257357, 3257358, JP-A-50-51197, JP-B52-17880, and 63-152628, etc. It is done.

The polyphenylene ether resin (C) used in the present invention may contain other various phenylene ether units as a partial structure within the range not impairing the effects of the present invention. Examples of the phenylene ether unit include a 2- (dialkylaminomethyl) -6-methylphenylene ether unit and a 2- (N-alkyl-N-phenylaminomethyl) -6-methylphenylene ether unit. Further, a small amount of diphenoquinone or the like may be bonded to the main chain of the PPE resin. Furthermore, one of two carboxyl groups of maleic acid, fumaric acid, chloromaleic acid, cis-4-cyclohexene-1,2-dicarboxylic acid and acid anhydrides thereof, and these unsaturated dicarboxylic acids or General ones such as those in which two are esters, allyl glycidyl ether, glycidyl acrylate, glycidyl methacrylate, epoxidized natural oil, allyl alcohol, 4-penten-1-ol, 1,4-pentadien-3-ol, etc. Unsaturated alcohols of the formula C _n H _2n-3 OH (n is a positive integer), unsaturated alcohols such as the general formulas C _n H _2n-5 OH, C _n H _2n-7 OH (n is a positive integer), etc. PPE resin modified by the above may be used. These modified PPE resins may be used alone or in combination of two or more.

  The molecular weight (number average molecular weight determined by gel permeation chromatography) of the polyphenylene ether resin (C) used in the present invention is usually 1,000 to 100,000, preferably 6,000 to 60,000. The reduced viscosity (measured with 0.5 g / dl chloroform solution, 30 ° C., Ubbelohde type viscosity tube) of the PPE resin (A) is usually in the range of 0.30 dl / g to 0.55 dl / g, preferably Is in the range of 0.35 dl / g to 0.50 dl / g. In the present invention, even a blend of two or more polyphenylene ether resins (C) having different reduced viscosities can be used.

  The polyphenylene ether resin (C) used in the present invention can be adjusted by melt kneading with a styrene resin in advance in order to stabilize the extrusion process at a low temperature.

  When the total of the impact-resistant styrene resin (A), polylactic acid (B), and polyphenylene ether resin (C) is 100% by mass, the content of each component is as follows. A) is preferably in the range of 50 to 90% by mass, polylactic acid (B) in the range of 5 to 35% by mass, and polyphenylene ether-based resin (C) in the range of 5 to 40% by mass. When the polylactic acid (B) exceeds 35% by weight, the Vicat softening point temperature and the heat distortion temperature of the resin composition may be lower than those of the impact-resistant styrenic resin, resulting in insufficient heat resistance as a final molded product. There is a fear. Moreover, when the amount of polylactic acid (B) is less than 5% by weight, the blending amount is small, so that it is difficult to differentiate from petroleum-derived resins from the viewpoint of environmental friendliness. If the polyphenylene ether-based resin (C) exceeds 40% by mass, the heat resistance is high, and stretching and secondary processing may be difficult. On the other hand, when the polyphenylene ether-based resin (C) is less than 5% by weight, the heat resistance may be insufficient depending on the application. The application is not sufficient and not preferable.

  In the present invention, the impact-resistant styrenic resin (A), polylactic acid (B), and polyphenylene ether resin (C) are blended and used. An agent may be used in combination.

  Examples of the various additives include an antistatic agent, an antioxidant, an ultraviolet absorber, a lubricant, an anti-blocking agent, and a heat stabilizer.

  The styrene-based stretched sheet of the present invention uses the above resin composition and performs biaxial stretching in the longitudinal direction and the width direction. By passing through the stretching step, the resin molecular chains are arranged, and the strength and oil resistance of the molded product can be improved.

  In addition, the heat shrinkage stress (ORS) of the biaxially stretched sheet is the maximum value of the stress developed at a sheet temperature of 120 ° C. by dry heating in accordance with ASTM D1504. It is preferably 2 to 1.0 MPa. If the heat shrinkage stress is small, the strength of the molded product may be insufficient, and if the heat shrinkage stress is large, there may be a problem in mold reproducibility during secondary molding.

  Although it does not specifically limit about the thickness of the styrene-type stretched sheet of this invention, From the viewpoint of the handleability at the time of obtaining a molded article by secondary processing, and the intensity | strength as a molded article, it is the range of 70-500 micrometers. It is preferable to make it become, and it is more preferable that it is the range of 100-300 micrometers.

  The styrene-based stretched sheet of the present invention can be obtained by uniformly mixing a solution obtained by dissolving each of the above components in a solvent, removing the solvent from the solution, and then forming a film. It is preferable to employ a melt film-forming method, which is a practical production method, without requiring steps such as dissolution and solvent removal. The melt film-forming method is a method for producing a sheet by melting and kneading each component. The melt film forming method is not particularly limited, and after obtaining a resin composition using various commonly used mixers such as a kneader, a roll mill, a Banbury mixer, a single-screw or twin-screw extruder, it is melted. Examples thereof include a method in which the mixed resin is introduced into a slit-shaped base, extruded into a sheet shape on a cooling casting drum, and a sheet is obtained using a T-die method, a touch roll casting method, or the like. Among these melt film forming methods, from the viewpoint of productivity, a method of forming a sheet using a single-screw extruder or a twin-screw extruder is preferable, and in terms of mixing properties, a sheet is formed using a twin-screw extruder. The method is further preferred.

  The order of mixing the resins is not particularly limited. For example, the impact-resistant styrene resin (A), the polylactic acid (B), and the polyphenylene ether resin (C) are dry blended and then supplied to a melt kneader. The method, or after preparing a masterbatch in which the impact-resistant styrene resin (A) and the polyphenylene ether resin (C) are melt-kneaded in advance, the masterbatch and polylactic acid (B) are melt-kneaded, and then a film is formed After preparing a master batch of homopolystyrene (GPPS) and polyphenylene ether resin (C) in advance, after melt-mixing the impact-resistant styrene resin (A) and polylactic acid (B) and the adjusted master batch And a method of forming a film.

  In addition, if necessary, a method of melt-kneading other additives at the same time, or preparing a master batch in which an impact-resistant styrene resin (A) and other additives are melt-kneaded in advance, A method of melt kneading the impact styrene resin (A), the polylactic acid (B), and the polyphenylene ether resin (C) may be used.

  Further, the temperature at which each component is melt-kneaded is preferably in the range of 180 ° C. to 260 ° C., from the viewpoint of preventing the deterioration of polylactic acid (B), and polylactic acid (B) and an impact-resistant styrene resin. From the viewpoint of kneadability of (A), the temperature at which each component is melt-kneaded is more preferably in the range of 200 ° C to 250 ° C.

  The draw ratio of the styrene-based stretched sheet is 1.3 to 8.0 times in at least one direction, preferably 1.7 to 6.0 times, and more preferably 1.5 to 4.0 times. . Moreover, extending | stretching temperature is the range of 70-150 degreeC. The styrene-based stretched sheet is preferably cooled below the stretching temperature from the viewpoint of preventing the orientation due to stretching from being relaxed after stretching and from the viewpoint of preventing the deterioration of formability due to the progress of crystallization. More preferably, the cooling is performed.

  A preferable example of the stretching conditions of the styrene-based stretched sheet is to roll-stretch 2.0 to 2.5 times and then produce a 0.21 mm styrene-stretched sheet that is tenter-stretched 2.0 to 2.5 times. The tenter stretching temperature is 80 to 140 ° C, and the cooling temperature is 40 to 70 ° C.

  Moreover, when changing a draw ratio from 2.5 times to 3.0 times, in order to obtain the same ORS sheet, it is preferable to raise the drawing temperature by 2 to 7 ° C. as a rough guide.

  In addition, when the surface is coated with a surfactant or the like in order to impart antistatic properties or antifogging properties to the resulting styrene-based stretched sheet, at least one surface of the stretched sheet is adjusted to an appropriate concentration. Examples include a method in which an aqueous solution such as a surfactant is applied by various methods such as a squeeze roll coater, an air knife coater, a knife coater, a spray coater, a gravure roll coater, and a bar coater, and then the applied aqueous solution is dried. In particular, from the viewpoint of improving the uniformity of the coating film, it is preferable to apply a surfactant or the like by the above method after corona treatment of the sheet surface. The strength of the corona treatment is preferably adjusted so that the contact angle with water is 80 to 30 °, more preferably the contact angle is 70 to 35 °. The preferred upper limit of the contact angle between the surface of the sheet and water is a value for improving the uniformity of the coating film, and the preferred lower limit of the contact angle is a value for preventing blocking when the sheet is rolled up. It is.

  The styrene-based stretched sheet obtained above can be secondarily processed by thermoforming into a molded product. As the thermoforming method, a hot plate contact heat forming method, a vacuum forming method, a vacuum / pressure forming method, a plug assist forming method, or the like is preferably used. The hot plate contact heating molding method is particularly preferable from the viewpoint of the uniformity of the thickness of the molded product and the production efficiency of the molded product, but when the transparency is particularly important, the vacuum molding method by indirect heating or the vacuum / pressure forming method is used. In addition, when performing deep drawing, a plug assist molding method can be employed.

  Secondary molding of the styrene-based stretched sheet using these molding methods may be performed continuously using a sheet roll, or may be molded for each shot using a cut plate sheet. Hereinafter, an example of preferable molded article manufacturing conditions will be given.

  Preferred hot plate temperature conditions for molding the styrene stretched sheet of the present invention by hot plate contact heating molding method include mold reproducibility and molding cycle viewpoint (lower limit), transparency of the molded product, From the viewpoint of the occurrence of raindrops (upper limit), the hot plate temperature is set to the Vicat softening temperature of the resin mixture +10 to 50 ° C, more preferably +15 to 40 ° C, and further preferably +20 to 35 ° C. In addition, the heating time (the time for which the sheet is brought into contact with the hot plate in vacuum and / or compressed air and the total delay time until the sheet is vacuumed and / or compressed in order to extend the sheet to the mold) 0.5-15.0 seconds are preferable.

  The shape of the molded product is not particularly limited, such as container lids, trays, food packs, blister packs, various other packs, cases, etc., but the moldability and oil resistance characteristic of the styrene stretched sheet of the present invention and the molded products thereof are not limited. From the viewpoint of impact resistance, it is preferably for food packaging, and particularly preferably used as a container tray.

  In particular, from the viewpoint of excellent oil resistance, a molded product obtained from the stretched sheet of the present invention can be suitably used even if it contains an oil component as a food product.

  EXAMPLES Hereinafter, although an Example is given and this invention is further demonstrated, this invention is not limited to these Examples at all. Unless otherwise indicated, both parts and% are based on mass.

  The thermal shrinkage stress, oil resistance, molding strength, and heat resistance of the obtained sheet were measured and evaluated by the following methods.

(1) Thermal contraction stress (ORS)
Measurement was performed in accordance with ASTM D-1504.

(2) Oil resistance The obtained styrene-based stretched sheet was cut into a strip of 100 × 20 mm, wound around a paper tube having a diameter of 90 mm, and edible oil (white F-2: manufactured by Fuji Seiki Co., Ltd.) was applied. It left still with the constant temperature apparatus of ° C, and time for a crack to enter into a strip by time-dependent change was checked. In addition, what did not change even if 24 hours (1440 minutes) passed was set to 1440 minutes or more.

(3) Molding strength (folding strength)
Based on JIS P8115, when the average of the vertical direction and the horizontal direction is less than 10 times, x is 10 times or more to less than 15 times, and 15 times or more is ◎.

(4) Formability and heat resistance A container having a depth of 27 mm and an opening of 95 mm × 95 mm is heated and heated by a hot plate contact method (heating temperature 1.2 seconds, molding delay time 1.5 seconds, molding time 2.0 seconds, heating For molded products obtained with a pressure of 0.1 MPa, a molding pressure of 0.4 MPa, and a mold temperature of 50 ° C., those that could be molded without surface roughness occurred, and surface roughness and other molding defects occurred. The thing was set as x. Furthermore, after leaving for 5 minutes in a 75 degreeC hot air dryer, the external appearance was visually observed. The case where there was no external deformation was indicated as ◯, the case where there was a partial deformation was indicated as Δ, and the case where there was a large deformation was indicated as ×.

(5) Fluidity The fluidity was measured at 200 ° C. and 5 kg load for impact-resistant styrene resin and general-purpose polystyrene (GPPS), and at 210 ° C. and 2.16 kg load for polylactic acid.

The following were used as impact-resistant styrene resin (A).
(A-1): Styrenic resin having a fluidity of 2.0 g / 10 min and a rubber component content of 7% in the resin (A-2): Fluidity of 4.0 g / 10 min, containing a rubber component in the resin Styrenic resin having an amount of 10% (A-3): styrene resin having a fluidity of 10.0 g / 10 min and a rubber component content of 3% in the resin

The method for synthesizing the resin is as follows.
(A-1): 90 parts of styrene monomer, 10 parts of toluene, 6 parts of butadiene rubber, 300 ppm of t-butyl peroxybenzoate (monomer ratio), and 1.5 hours at 130 ° C. in a stirred reaction vessel The reaction was carried out at 140 ° C. to 180 ° C. for 3.5 hours. And purified by purification.

  (A-2): Under the conditions of (A-1), the above resin was obtained by synthesis under the same conditions except that the butadiene rubber was changed to 8%.

  (A-3): The above resin was obtained by synthesis under the same conditions except that the butadiene rubber was changed to 2.5% under the conditions of (A-1).

  As polylactic acid (B), 4032D (flowability 7 g / 10 min., D-form: 1.4%, weight average molecular weight: 180,000) manufactured by Nature Works was used.

  In this example, the polyphenylene ether resin (C) prepared by the following method was used. PX-100F (poly (2,6-dimethyl-1,4-phenylene) ether resin, 0.38 dl / g (30 ° C. in chloroform)) and general-purpose polystyrene (GPPS: MFR: 5.0 g) manufactured by Mitsubishi Engineering Plastics / 10 min. (200 ° C., 5 kg load)) was dry blended at a weight ratio of 70:30, and a masterbatch was prepared using a twin screw extruder (melting temperature 300 ° C.).

Example 1
Impact-resistant styrene resin (A-1) / polylactic acid (B) / polyphenylene ether resin (C) = 55/25/20 twin screw extruder (manufactured by Nippon Steel) TEX30α-31.5BW-5V), melt, knead, extrude the sheet from the T-die, cool the sheet with a roll, reheat, and then roll the sheet in the sheet flow direction due to the speed difference of the roll group (MD) was stretched 2.0 times. Further, the sheet was stretched 2.0 times in a direction orthogonal to the sheet flow direction (referred to as TD) by a tenter to obtain a sheet having a thickness of 0.25 mm.

Example 2
A sheet was obtained by the same method except that the draw ratio of TD and MD in Example 1 was 2.5 times.

Example 3
A sheet was obtained in the same manner as in Example 1 except that the impact-resistant styrene resin was changed to (A-2).

Example 4
A sheet was obtained by the same method except that the stretching ratio of TD and MD was 2.5 times under the conditions of Example 3.

Example 5
In Example 1, a sheet was obtained by the same method except that the impact-resistant styrene resin was changed to (A-3).

Example 6
A sheet was obtained by the same method except that the stretching ratio of TD and MD was 2.5 times under the conditions of Example 5.

Example 7
A sheet was obtained in the same manner as in Example 1 except that the ratio was changed to the ratio of impact-resistant styrene resin (A-1) / polylactic acid (B) / polyphenylene ether resin (C) = 75/5/20. It was.

Example 8
A sheet was obtained by the same method except that the draw ratio of TD and MD in Example 7 was 2.5.

Example 9
In Example 7, a sheet was obtained by the same method except that the impact-resistant styrenic resin was changed to the ratio (A-2).

Example 10
A sheet was obtained by the same method except that the stretching ratio of TD and MD was 2.5 times under the conditions of Example 9.

Example 11
In Example 7, a sheet was obtained by the same method except that the impact-resistant styrene resin was changed to (A-3).

Example 12
A sheet was obtained by the same method except that the stretching ratio of TD and MD was 2.5 times under the conditions of Example 11.

Example 13
A sheet was obtained in the same manner as in Example 1 except that the ratio was changed to the ratio of impact-resistant styrene resin (A-1) / polylactic acid (B) / polyphenylene ether resin (C) = 55/5/40. It was.

Example 14
A sheet was obtained by the same method except that the draw ratio of TD and MD in Example 13 was 2.5.

Example 15
In Example 13, a sheet was obtained by the same method except that the impact-resistant styrene resin was changed to (A-2).

Example 16
A sheet was obtained by the same method except that the stretching ratio of TD and MD was 2.5 times under the conditions of Example 15.

Example 17
In Example 13, a sheet was obtained by the same method except that the impact-resistant styrene resin was changed to (A-3).

Example 18
A sheet was obtained by the same method except that the stretching ratio of TD and MD was 2.5 times under the conditions of Example 17.

Comparative Example 1
In Example 1, a sheet was obtained by the same method except that the impact-resistant styrene resin (A-1) was used alone.

Comparative Example 2
A sheet was obtained in the same manner as in Example 1 except that the film was not stretched (TD and MD stretch ratio: 1.0).

Comparative Example 3
A sheet was obtained under the same conditions as in Example 1, except that the impact-resistant styrene resin (A-1) / polylactic acid (B) = 65/35.

  The evaluation results are shown in Tables 1-3.

Claims (9)

A styrene-based stretched sheet obtained by biaxially stretching a styrene-based resin composition containing an impact-resistant styrene-based resin (A), polylactic acid (B), and polyphenylene ether-based resin (C). As a mass ratio represented by (A) / (B) / (C), the use ratio of the impact-resistant styrene resin (A), polylactic acid (B), and polyphenylene ether resin (C) is 50 to 90. The styrene-based stretched sheet according to claim 1, which is in a range of / 5 to 35/5 to 40. The stretched styrene-based sheet according to claim 1 or 2, wherein the impact-resistant styrene-based resin (A) is obtained by graft polymerization of a rubbery polymer on a continuous phase composed of a polymer of styrene alone. The styrene-based stretched sheet according to claim 3, wherein the content of the rubber component in the impact-resistant styrene-based resin (A) is 2.0 to 15% by mass. 5. The styrene resin composition is a biaxially stretched stretch ratio of 1.3 to 8.0 times in the longitudinal direction and 1.3 to 8.0 times in the transverse direction. 5. Styrene-based stretched sheet. The styrene-based stretched sheet according to any one of claims 1 to 5, wherein the heat shrinkage stress in the longitudinal direction is 0.2 to 1.0 MPa, and the heat shrinkage stress in the transverse direction is 0.2 to 1.0 MPa. A molded article obtained by molding the styrene-based stretched sheet according to any one of claims 1 to 6 by a thermoforming method. The molded article according to claim 7, which is used for food packaging. The molded article according to claim 8, wherein the food contains an oil component.