WO2020075755A1 - ポリプロピレンシートの製造方法 - Google Patents

ポリプロピレンシートの製造方法 Download PDF

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Publication number
WO2020075755A1
WO2020075755A1 PCT/JP2019/039822 JP2019039822W WO2020075755A1 WO 2020075755 A1 WO2020075755 A1 WO 2020075755A1 JP 2019039822 W JP2019039822 W JP 2019039822W WO 2020075755 A1 WO2020075755 A1 WO 2020075755A1
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WO
WIPO (PCT)
Prior art keywords
sheet
film
thickness
polypropylene
biaxially stretched
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
Application number
PCT/JP2019/039822
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English (en)
French (fr)
Japanese (ja)
Inventor
中島　武
正幸 池田
片桐　章公
Current Assignee (The listed assignees may be inaccurate. Google has not performed a legal analysis and makes no representation or warranty as to the accuracy of the list.)
SunAllomer Ltd
Original Assignee
SunAllomer Ltd
Priority date (The priority date 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 date listed.)
Filing date
Publication date
Application filed by SunAllomer Ltd filed Critical SunAllomer Ltd
Priority to BR112021006684-5A priority Critical patent/BR112021006684B1/pt
Priority to EP19871892.6A priority patent/EP3865285A4/en
Priority to MX2021004089A priority patent/MX2021004089A/es
Priority to JP2020551196A priority patent/JP7279066B2/ja
Priority to US17/283,938 priority patent/US12172359B2/en
Priority to CN201980066336.9A priority patent/CN112955308B/zh
Priority to CA3115748A priority patent/CA3115748C/en
Publication of WO2020075755A1 publication Critical patent/WO2020075755A1/ja
Anticipated expiration legal-status Critical
Priority to US18/903,699 priority patent/US20250018630A1/en
Ceased legal-status Critical Current

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    • B29—WORKING OF PLASTICS; WORKING OF SUBSTANCES IN A PLASTIC STATE IN GENERAL
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    • B29C48/00—Extrusion moulding, i.e. expressing the moulding material through a die or nozzle which imparts the desired form; Apparatus therefor
    • B29C48/16—Articles comprising two or more components, e.g. co-extruded layers
    • B29C48/18—Articles comprising two or more components, e.g. co-extruded layers the components being layers
    • B29C48/21—Articles comprising two or more components, e.g. co-extruded layers the components being layers the layers being joined at their surfaces
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    • B32B27/16—Layered products comprising a layer of synthetic resin specially treated, e.g. irradiated
    • B—PERFORMING OPERATIONS; TRANSPORTING
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    • B29C48/00—Extrusion moulding, i.e. expressing the moulding material through a die or nozzle which imparts the desired form; Apparatus therefor
    • B29C48/001—Combinations of extrusion moulding with other shaping operations
    • B29C48/0018—Combinations of extrusion moulding with other shaping operations combined with shaping by orienting, stretching or shrinking, e.g. film blowing
    • B—PERFORMING OPERATIONS; TRANSPORTING
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Definitions

  • the present invention relates to a method for manufacturing a polypropylene sheet.
  • Extended polypropylene film is used in fields where high transparency and mechanical properties are required in addition to high heat resistance.
  • its thickness is less than 150 ⁇ m, which limits its use. Therefore, if the thickness of the stretched film can be increased, it is expected to expand to other uses.
  • Patent Document 1 discloses that a sheet having a certain thickness or more can be manufactured by laminating a plurality of polypropylene uniaxially stretched films and heat-sealing them.
  • Patent Document 2 it is possible to provide a polypropylene sheet having excellent transparency and mechanical properties by laminating a plurality of biaxially oriented polypropylene films having specific higher order structural parameters and heating and fusing them. It is disclosed.
  • an object of the present invention is to provide a production method for producing a polypropylene sheet having excellent transparency and mechanical properties with high productivity.
  • a method for producing a polypropylene sheet having a thickness of 0.5 to 5 mm comprising: A precursor in which a first biaxially oriented polypropylene film having a thickness of less than 0.15 mm and a melting point Tmh and a second biaxially oriented polypropylene film having a thickness of less than 0.15 mm and a melting point Tml are laminated alternately.
  • Step 1 of preparing Including a step 2 of bringing a heating element into contact with the outermost layer of the precursor to heat-bond the layers of the film together Tmh-Tml ⁇ 8 (° C.), (However, these melting points are obtained by using DSC at a temperature rising rate of 10 ° C./min from 30 ° C. to 230 ° C.) Production method.
  • Tm out- T ⁇ 4 (° C) The method for producing a sheet according to [1].
  • the ratio Dh / Dl of the layer thickness Dh resulting from the first biaxially oriented polypropylene film and the layer thickness Dl resulting from the second biaxially oriented polypropylene film is 1
  • a raw material sheet having a plurality of layers is prepared by coextruding a raw material of the first biaxially oriented polypropylene film and a raw material of the second biaxially oriented polypropylene film, and The production method according to any one of [1] to [5], including a step of preparing the precursor by biaxial stretching.
  • a method for producing a molded article comprising preparing a polypropylene sheet by the method according to any one of [1] to [6] above, and molding the polypropylene sheet.
  • the present invention can provide a manufacturing method for manufacturing a polypropylene sheet having excellent transparency and mechanical properties with high productivity.
  • X to Y includes its extreme values, that is, X and Y.
  • the sheet means a film-like member having a thickness of 150 ⁇ m or more, and the film means a film-like member having a thickness of less than 150 ⁇ m.
  • the method for manufacturing a sheet of the present invention comprises a first biaxially oriented polypropylene film having a thickness of less than 0.15 mm and a melting point Tmh, and a second biaxially oriented polypropylene film having a thickness of less than 0.15 mm and a melting point Tml.
  • the method includes a step 1 of preparing a precursor in which stretched polypropylene films are alternately laminated, and a step 2 of bringing a heating body into contact with the outermost layer of the precursor to heat-bond the layers of the film.
  • These melting points satisfy Tmh-Tml ⁇ 8 (° C.). When the melting point difference is in this range, the adhesion between layers becomes good.
  • the melting point difference is preferably 10 (° C.) or more.
  • the upper limit of the melting point difference is not limited, it is preferably 40 (° C.) or less from the viewpoint of polypropylene production.
  • each step will be described.
  • Step 1 a precursor in which the first biaxially oriented polypropylene film and the second biaxially oriented polypropylene film are alternately laminated is prepared. Since the precursor includes a plurality of the films, a plurality of layers are present. It is not necessary that all the layers be fused, but one or several layers may be fused. For example, when laminating the first biaxially oriented polypropylene film and the second biaxially oriented polypropylene film one by one, it is preferable that all the layers in the precursor are not fused. Further, as will be described later, when a coextruded film of a first biaxially oriented polypropylene film and a second biaxially oriented polypropylene film is used, one or some layers in the precursor are fused.
  • a first biaxially oriented polypropylene film (for convenience, hereinafter also referred to as “F1”) and a second biaxially oriented polypropylene film (for convenience, hereinafter also referred to as “F2”) are separately prepared, and these are alternated. It can be carried out by stacking on.
  • the precursor can be prepared by stacking as F1 / F2 / F1 / F2 / F1. In this case, it is preferable that one or some of all the layers are not fused. From the viewpoint of enhancing the heat resistance of the obtained sheet, both outermost layers are preferably F1.
  • the biaxially stretched film having a thickness of less than 0.15 mm can be obtained by biaxially stretching polypropylene or a composition containing the polypropylene and an additive by a known method.
  • the polypropylene or the like can be extrusion-molded or press-molded to obtain an unstretched sheet, and the sheet can be biaxially stretched to obtain a biaxially stretched film.
  • the thickness of the film is not limited as long as it is less than 0.15 mm, it is preferably 0.12 mm or less, more preferably 0.10 mm or less from the viewpoint of easy handling and the like.
  • the lower limit of the thickness is not limited, it is preferably 0.01 mm or more, more preferably 0.03 mm or more.
  • step 2 can also be performed using a coextruded film of F1 and F2.
  • step 2 can be simplified.
  • a raw material sheet having a plurality of layers is prepared by coextruding a raw material of F1 and a raw material of F2, and biaxially stretched to prepare a precursor in which F1 and F2 are alternately laminated. it can.
  • the number of precursor layers is not limited, but two or three layers are preferable.
  • a coextruded bilayer biaxially stretched film of F1 / F2 or a coextruded trilayer biaxially stretched film of F2 / F1 / F2 can be obtained and a desired number of the films can be superposed.
  • the following precursor can be prepared. [F1 / F2] / [F1 / F2] / [F1 / F2] / F1 / F2] / F1
  • the raw material of F1 is a material capable of forming F1, and may have any shape such as a film, a sheet, a pellet, and a powder. The same applies to the raw material of F2.
  • the precursor may include a case where F1s or F2s are integrated by heat fusion in step 2 described later, and finally a structure in which F1s and F2s are alternately laminated is formed.
  • the following precursor may be prepared.
  • Each film can be placed in any direction.
  • the orientation direction in the sheet plane can be adjusted by the placement of the film.
  • the number of laminated films is appropriately adjusted. Details of polypropylene and additives will be described later.
  • Step 2 a heating element is brought into contact with the outermost layer of the precursor to heat and fuse the layers.
  • the melting point Tm out of the outermost layer and the temperature T of the heating body satisfy the relationship of Tm out ⁇ T ⁇ 4 (° C.). By satisfying the relationship, the layers can be fused well. From this viewpoint, it is more preferable that the temperature difference is 6 ° C. or more.
  • the upper limit of the temperature difference is not limited, it is preferably 40 ° C. or lower from the viewpoint of polypropylene production.
  • T can be measured by any method, it is preferable to measure T using a non-contact thermometer such as a radiation thermometer.
  • Tm out corresponds to the melting point of the single-layer film arranged in the outermost layer.
  • the melting point is defined as the peak temperature of the melting curve obtained by measuring with DSC from 30 ° C. to 230 ° C. at a temperature rising rate of 10 ° C./min.
  • the temperature of the heating element is not limited, it is preferably about 120 to 190 ° C, more preferably 140 to 170 ° C, still more preferably 150 to 165 ° C.
  • this step is continuously performed using a heating roll as a heating element.
  • the precursor is passed between two heated rolls to fuse the layers.
  • Two rolls may be set as one set and a heating roll obtained by combining two or more sets of rolls may be used as a heating body for fusion.
  • the pressure applied at this time is appropriately adjusted.
  • the take-up speed in the roll forming is not limited, but is preferably about 0.05 to 10 m / min.
  • pressure contact forming As methods other than roll forming, pressure contact forming, fusion forming, etc. may be mentioned. Further, when the film is heat-fused, it is preferable to apply pressure in order to suppress heat shrinkage and further promote orientation. The pressure at that time is adjusted according to the fusion temperature.
  • the production method of the present invention may further include known steps such as cooling the sheet obtained in the previous step.
  • the cooling method is not limited, and examples thereof include a method of allowing to cool at room temperature and a method of cold pressing at room temperature or 10 to 20 ° C.
  • the sheet obtained by the production method of the present invention has good adhesion between films and almost no discontinuity between layers. Therefore, it can be handled as an integrated sheet. It was not industrially practical to obtain a biaxially oriented sheet having a thickness of 0.5 mm or more by the conventional method from the viewpoint of cost, etc., but according to the present invention, the thickness is 0.5 mm or more and bidirectional or more. A sheet having an orientation of can be industrially manufactured.
  • various molded bodies can be obtained.
  • the secondary forming method include known press forming, hot plate forming, stretch forming, rolling forming, drawing forming, pressure contact forming, fusion forming, vacuum forming, pressure forming, vacuum pressure forming.
  • a special film may be attached to the outermost surface of the sheet obtained by the production method of the present invention for the purpose of decorating, surface modification and the like.
  • the film to be attached include an anti-fog film, a low temperature seal film, an adhesive film, a printing film, an embossed film, a retort film and the like.
  • the thickness of the outermost film is not particularly limited, but if it is too thick, the characteristics of the sheet obtained in the present invention may be impaired, and the special film is generally costly and economically undesirable. Therefore, it is preferably thin.
  • a special film can be laminated on the surface of the film arranged as the outermost layer.
  • the sheet obtained by the production method of the present invention may be coated to form a coated sheet having a coating film on the sheet.
  • the type of coating film is not limited, and is not limited as long as it is usually used in the field of coating.
  • the coating film used for car body painting is preferable.
  • Preferred coatings include epoxy coatings, urethane coatings, polyester coatings and the like.
  • a lower layer coating film (primer coating film), an intermediate layer coating film and an upper layer coating film (clear coating film) may be provided.
  • the surface to be coated has a functional group.
  • the method for applying a functional group to the surface of the sheet obtained by the production method of the present invention is not limited.
  • an oxygen-containing functional group can be imparted to the surface by subjecting the sheet obtained by the production method of the present invention to plasma treatment or corona treatment.
  • a functional group can be imparted by preparing a polypropylene film having a functional group and laminating it with the above-mentioned film so that the functional group-containing film becomes the outermost layer in the laminating step.
  • the latter method will be described.
  • a polypropylene film having an oxygen-containing functional group can be obtained by molding a known polypropylene such as maleic anhydride modified polypropylene or epoxy modified polypropylene into the film.
  • the thickness of the functional group-containing film is not limited, it is preferably less than 150 ⁇ m.
  • the functional group-containing film may or may not be biaxially stretched.
  • a polypropylene film having a functional group and a polypropylene film having no functional group may be laminated at the same time, or a polypropylene film having no functional group may be laminated in advance to produce a sheet, A polypropylene film having a functional group may be laminated on the surface of the.
  • a method of laminating at the same time considering workability is preferable.
  • the polypropylene sheet obtained by the production method of the present invention (also referred to as “sheet obtained by the production method of the present invention”) has a thickness of 0.5 to 5 mm.
  • the thickness may be appropriately adjusted depending on the application, and may be, for example, 0.7 mm or more or 1 mm or more. Further, the thickness may be 3 mm or less or 1 mm or less.
  • the sheet obtained by the manufacturing method of the present invention has a multilayer structure in which first layers having a high melting point Tmh and second layers having a low melting point Tml are alternately laminated. Since the layers are fused, the sheet obtained by the production method of the present invention is an integrated sheet. Specifically, as to whether the layers of the sheet are fused and integrated with each other, or whether peeling occurs due to application of a slight force due to insufficient fusion, as shown in FIG. It can be confirmed by observing the cross section.
  • FIG. 1 (1) shows that the first layer and the second layer are well fused.
  • FIG. 1 (2) shows a state in which the layers of the sheet composed of the plurality of first layers are completely peeled, partially peeled, and well fused.
  • Dh / Dl of the thickness Dh of the first layer and the thickness Dl of the second layer when the value is small, the fusion property between the layers is excellent, and when the value is large, the rigidity of the obtained sheet is high.
  • Dh / Dl is preferably 1 to 30, more preferably 1 to 25, and further preferably 4 to 25.
  • the number of layers depends on the thickness of the monolayer film, but in one aspect, it is preferable that the total of the first layer and the second layer having a thickness of about 0.01 to 0.1 mm be about 15 to 100 layers. At this time, both outermost layers are preferably the first layer having a high melting point.
  • Tmh and Tml are not limited, but in one embodiment, Tmh is preferably 160 to 180 ° C, and Tml is preferably 130 to 150 ° C.
  • the sheet obtained by the production method of the present invention in the azimuth angle of scattering in the meridian (Z) direction in the two-dimensional profile of small-angle X-rays measured by making X-rays (wavelength: 0.154 nm) incident from the X direction.
  • FIG. 2 illustrates a sheet obtained by laminating a plurality of films.
  • the scattering peaks in the equatorial direction are derived from the crystalline lamellae regularly arranged in the in-plane direction of the sheet.
  • the presence of regularly arranged crystalline lamellas increases the equatorial scattering intensity.
  • the streak in the meridian direction is mainly derived from the reflection of the surface of the gap remaining between the layers of the biaxially stretched film laminated in the Z direction. Therefore, I X L increases when increases or is maintained in the orientation crystal sheet biaxially stretched film.
  • the fusion between the layers of the biaxially stretched film is sufficient, the gap surface remaining between the layers is reduced, and as a result, the streak of I X V is reduced.
  • I X L is large
  • I X V is small
  • the transparency and mechanical properties of the sheet are improved.
  • I X L is large
  • I X V is small
  • the transparency and mechanical properties of the sheet are improved.
  • a small lamella grows in a direction substantially perpendicular to the parent lamella.
  • the long-period scattering peak derived from the daughter lamella is observed as I X V.
  • Figure 4 is a graph showing the relationship between integrated intensity I X L and 2 ⁇ in azimuth of small-angle X Scattering 2-dimensional profile of Comparative Example 8 and Example 10.
  • Tm out -T ⁇ 4 (°C) Tm out -T ⁇ 4 (°C) compared to the sheet of Comparative Example 8 not satisfying the more and more sequences crystals lamellae (parent It can be seen that there is a lamella).
  • FIG. 5 is a diagram showing a relationship between integrated intensity I X V and 2 ⁇ at an azimuth angle of a small-angle X-scattering two-dimensional profile in Example 10 and Comparative Example 8.
  • the sheet obtained by the production method of the present invention has excellent mechanical properties.
  • the sheet obtained by the production method of the present invention has a tensile elastic modulus (JIS K7161-2) of 2,500 MPa or more.
  • the sheet obtained by the production method of the present invention is also excellent in cold shock resistance.
  • the sheet obtained by the production method of the present invention has a surface impact strength of ⁇ 5 J or higher ( ⁇ 30 ° C., JIS K7211-2).
  • the sheet obtained by the production method of the present invention has excellent transparency.
  • the sheet obtained by the manufacturing method of the present invention has a total haze (ISO 14782) of 25% or less. The smaller the total haze of the sheet, the more excellent the transparency is, and preferably 20% or less.
  • the surface of the sheet obtained by the production method of the present invention can be provided with a functional group as described above.
  • a functional group an oxygen-containing functional group is preferable.
  • the oxygen-containing functional group include a carboxyl group, a carboxylate group, an acid anhydride group, a hydroxyl group, an aldehyde group and an epoxy group.
  • These functional groups improve the adhesion between the sheet obtained by the production method of the present invention and other materials.
  • the coated member obtained by the production method of the present invention having the functional group has excellent gasohol resistance, which is resistance to gasoline mixed with alcohol.
  • the acid anhydride group is preferable among the functional groups.
  • the functional group may be present on any surface of the sheet obtained by the production method of the present invention, but is preferably present on one side or both sides of the main surface.
  • the method of imparting a functional group is as described above.
  • polypropylene means a polymer containing polypropylene as a main component.
  • the polypropylene used for the first layer of the sheet obtained by the production method of the present invention is propylene homopolymer (HOMO), or 5.0% by weight or less of ethylene and at least one of C4 to C10- ⁇ olefin as a comonomer.
  • HOMO propylene homopolymer
  • a propylene random copolymer (RACO) containing is preferred. RACO having a low content of HOMO or comonomer is particularly preferable because of its excellent rigidity and transparency.
  • RACO containing 15% by weight or less of ethylene and at least one of C4 to C10- ⁇ olefins as a comonomer is preferable.
  • RACO having a high comonomer content is particularly preferable because it has excellent adhesion after fusion with the first layer.
  • polypropylenes can be manufactured according to a known method.
  • a polymerization catalyst of polypropylene a solid catalyst containing (A) magnesium, titanium, halogen, and an electron donor compound, a catalyst containing (B) an organoaluminum compound, and (C) an external electron donor compound
  • Metallocene catalysts are known as a polymerization catalyst of polypropylene.
  • Any catalyst can be used to produce the polypropylene of the present invention.
  • the electron donor compound (also referred to as “internal electron donor compound”) in the component (A) include phthalate compounds, succinate compounds, and diether compounds, and in the present invention, any internal electron donor compound is used.
  • a catalyst containing a succinate compound as an internal electron donor compound is preferable because the obtained polypropylene has a wide molecular weight distribution and good biaxial stretchability.
  • the sheet obtained by the production method of the present invention may contain a nucleating agent.
  • the amount of the nucleating agent is more than 0 parts by weight and not more than 1.0 parts by weight, preferably 0.05 to 0.5 parts by weight, based on 100 parts by weight of polypropylene.
  • the nucleating agent is an additive (transparent nucleating agent) used for controlling the size of the crystal component in the resin to be small and enhancing the transparency.
  • the nucleating agent is not particularly limited, and those commonly used in the art may be used, but nonitol nucleating agents, sorbitol nucleating agents, phosphate ester nucleating agents, triaminobenzene derivative nucleating agents, metal carboxylates.
  • salt nucleating agents and xylitol-based nucleating agents are preferably selected from salt nucleating agents and xylitol-based nucleating agents.
  • nonitol-based nucleating agent include 1,2,3-trideoxy-4,6: 5,7-bis-[(4-propylphenyl) methylene] -nonitol.
  • sorbitol-based nucleating agent include 1,3: 2,4-bis-o- (3,4-dimethylbenzylidene) -D-sorbitol.
  • the phosphoric acid ester-based nucleating agent include a phosphoric acid-2,2′-methylenebis (4,6-di-tert-butylphenyl) lithium salt-based nucleating agent.
  • the sheet obtained by the production method of the present invention includes an antioxidant, a chlorine absorber, a heat resistance stabilizer, a light stabilizer, an ultraviolet absorber, an internal lubricant, an external lubricant, an antiblocking agent, an antistatic agent, and an antifogging agent.
  • an antioxidant e.g., a chlorine absorber, a heat resistance stabilizer, a light stabilizer, an ultraviolet absorber, an internal lubricant, an external lubricant, an antiblocking agent, an antistatic agent, and an antifogging agent.
  • conventional additives commonly used in polyolefins such as agents, flame retardants, dispersants, copper damage inhibitors, neutralizers, plasticizers, crosslinkers, peroxides, oil extensions and other organic and inorganic pigments. You may stay.
  • the addition amount of each additive may be a known amount.
  • a synthetic resin or synthetic rubber other than polypropylene may be contained as long as the effect of the present invention is not impaired.
  • the sheet obtained by the production method of the present invention has a high degree of orientation and a specific higher order structural parameter in the in-plane direction, and has a small dependency of the degree of orientation in the thickness direction, so that it is lightweight as polypropylene. It has excellent mechanical properties.
  • the sheet obtained by the production method of the present invention also has excellent transparency. Therefore, it can be suitably used for food containers / lids, sundries, home electric appliances, daily necessities and the like. Further, by stacking and pressing or fusing a plurality of sheets obtained by the production method of the present invention, it is possible to obtain a thicker sheet or a larger molded body while maintaining the orientation and the like.
  • the sheet obtained by the manufacturing method of the present invention is also useful as an automobile part, an electric / electronic part, a housing member, a toy member, a furniture member, a building material member, an industrial material, a distribution material, an agricultural material, or the like.
  • a solid catalyst component (1) was prepared according to the preparation method described in Examples of JP-A-2011-500907. Specifically, it is as follows. 250 mL of TiCl 4 was introduced at 0 ° C. into a 500 mL 4-neck round bottom flask purged with nitrogen. With stirring, 10.0 g of finely spherical MgCl 2 .1.8C 2 H 5 OH (produced according to the method described in Example 2 of US Pat. No. 4,399,054, but operating at 3000 rpm instead of 10000 rpm).
  • the solid catalyst (1) obtained above, triethylaluminum (TEAL), and diisopropyldimethoxysilane (DIPMS) had a weight ratio of TEAL to solid catalyst (1) of 11, and a weight ratio of TEAL / DIPMS.
  • the catalyst system thus obtained was prepolymerized by holding it in liquid propylene in a suspended state at 20 ° C. for 5 minutes to obtain a prepolymerization catalyst (S).
  • the prepolymerization catalyst (S) is introduced into the polymerization reactor, propylene is supplied as a monomer, and a small amount of ethylene and a molecular weight modifier are added so that the ethylene concentration in the polymerization reactor is 0.118 mol% and the hydrogen concentration is 700 molppm. Was supplied as hydrogen.
  • a propylene-ethylene copolymer was synthesized by adjusting the polymerization temperature to 70 ° C. and the polymerization pressure to 3.0 MPa. With respect to 100 parts by weight of the obtained polymer, 0.2 parts by weight of an antioxidant (B225 manufactured by BASF) and 0.05 parts by weight of a neutralizing agent (calcium stearate manufactured by Tanan Chemical Co., Ltd.) were blended.
  • the mixture was stirred by a Henschel mixer for 1 minute and mixed.
  • the mixture is melt-kneaded at a cylinder temperature of 230 ° C. using an NVC ⁇ 50 mm single-screw extruder manufactured by Nakatani Machinery Co., Ltd., and the extruded strand is cooled in water, and then cut with a pelletizer to obtain a pelletized polymer composition (a).
  • Got The ethylene content of the polymer composition (a) was 0.5% by weight, and the MFR (temperature 230 ° C., load 2.16 kg) was 3.0 g / 10 minutes.
  • a raw sheet (size 10 cm) having a thickness of 1.25 mm from the polymer composition (a) at a forming temperature of 230 ° C. X 10 cm or more) was obtained. Then, the raw sheet was simultaneously biaxially stretched (5 times ⁇ 5 times) using a film stretching device (KARO-IV manufactured by Bruckner Co.) to obtain a biaxially stretched film A having a thickness of 50 ⁇ m.
  • a solid catalyst (2) was prepared by the method described in Example 1 of EP 674991.
  • the solid catalyst is obtained by supporting Ti and diisobutyl phthalate as an internal donor on MgCl 2 by the method described in the above patent publication.
  • Contact was performed at -5 ° C for 5 minutes.
  • Prepolymerization was carried out by holding the resulting catalyst system in suspension in liquid propylene for 5 minutes at 20 ° C.
  • the propylene-ethylene copolymer was obtained by adjusting the polymerization pressure at a polymerization temperature of 75 ° C., a hydrogen concentration of 0.44 mol% and an ethylene concentration of 1.07 mol%.
  • a polymerization temperature of 75 ° C. a hydrogen concentration of 0.44 mol% and an ethylene concentration of 1.07 mol%.
  • an antioxidant B225 manufactured by BASF
  • a neutralizing agent calcium stearate manufactured by Tanan Chemical Co., Ltd.
  • the mixture is melt-kneaded at a cylinder temperature of 230 ° C. using an NVC ⁇ 50 mm single-screw extruder manufactured by Nakatani Machinery Co., Ltd., and the extruded strand is cooled in water, and then cut with a pelletizer to obtain a pelletized polymer composition (b).
  • Got The polymer composition (b) contained 4.0% by weight of ethylene-derived units and had an MFR (temperature of 230 ° C., load of 2.16 kg) of 7.5 g / 10 minutes.
  • a raw sheet having a thickness of 1.25 mm (size 10 cm ⁇ ) from the polymer composition (b) at a forming temperature of 230 ° C. 10 cm or more) was obtained.
  • the original sheet was simultaneously biaxially stretched (5 ⁇ 5 times) by using a film stretching device (KARO-IV manufactured by Bruckner) to obtain a biaxially stretched film B having a thickness of 50 ⁇ m.
  • the polymer composition (c) was a propylene-ethylene-butene-1 copolymer (propylene: 90% by weight, ethylene: 4% by weight, butene: 6% by weight, and had an MFR at a temperature of 230 ° C. and a load of 2.16 kg. RACO with 5.5 g / 10 min and a density of 0.90 g / cm 3 ) was used.
  • a 25 mm ⁇ three-layer three-layer film / sheet molding machine (made by Thermo Plastics Industries Co., Ltd.) at a molding temperature of 230 ° C., from the polymer composition (c), a raw sheet having a thickness of 1.25 mm (size: 10 cm ⁇ 10 cm or more) was obtained.
  • the original sheet was simultaneously biaxially stretched (5 ⁇ 5 times) using a film stretching device (KARO-IV manufactured by Bruckner) to obtain a biaxially stretched film C having a thickness of 50 ⁇ m.
  • the propylene-ethylene copolymer was obtained by adjusting the polymerization pressure at a polymerization temperature of 75 ° C., a hydrogen concentration of 0.03 mol% and an ethylene concentration of 0.13 mol%.
  • a polymerization temperature of 75 ° C. a hydrogen concentration of 0.03 mol% and an ethylene concentration of 0.13 mol%.
  • an antioxidant B225 manufactured by BASF
  • a neutralizing agent calcium stearate manufactured by Tanan Chemical Co., Ltd.
  • the polymer composition (d) contained 0.5% by weight of an ethylene-derived unit and had an MFR (temperature: 230 ° C., load: 2.16 kg) of 2.5 g / 10 minutes.
  • a raw sheet (size: 10 cm ⁇ ) of a thickness of 1.25 mm from the polymer composition (d) at a molding temperature of 230 ° C. 10 cm or more) was obtained.
  • the original sheet was simultaneously biaxially stretched (5 ⁇ 5 times) using a film stretching device (KARO-IV manufactured by Bruckner) to obtain a biaxially stretched film D having a thickness of 50 ⁇ m.
  • the mixture was extruded at a cylinder temperature of 230 ° C. using a single-screw extruder (NVC manufactured by Nakatani Machinery Co., Ltd.) having a screw diameter of 50 mm, the strand was cooled in water, and then cut with a pelletizer to obtain a pelletized polymer composition.
  • (E) was obtained.
  • the ethylene-derived unit of the polymer composition (e) was 0% by weight, and the MFR (temperature 230 ° C., load 2.16 kg) was 10 g / 10 minutes.
  • a 25 mm ⁇ three-layer three-layer film / sheet molding machine (made by Thermo Plastics Industries Co., Ltd.) at a molding temperature of 230 ° C., from the polymer composition (d), a raw sheet having a thickness of 1.25 mm (size: 10 cm ⁇ 10 cm or more) was obtained.
  • the original sheet was simultaneously biaxially stretched (5 times ⁇ 5 times) by using a film stretching device (KARO-IV manufactured by Bruckner) to obtain a biaxially stretched film E having a thickness of 50 ⁇ m.
  • the original sheet is simultaneously biaxially stretched (5 ⁇ 5 times) using a film stretching device (KARO-IV manufactured by Bruckner Co.), and biaxially stretched films AC, AD, DB, DC and EB-1 having a thickness of 50 ⁇ m. , EB-2 was obtained.
  • the thickness ratio was 85/15 for EB-1 and 90/10 for AC, AD, DB, DC and EB-2.
  • Example 1 Eleven biaxially stretched films A and ten biaxially stretched films B were alternately laminated to prepare a precursor in which both outermost layers were the biaxially stretched film A. Using a roll forming machine (induction heating jacket roller manufactured by Tokuden Co., model JR-D0-W, roll diameter 200 mm ⁇ ⁇ 2 rolls, roll surface length 410 mm) as a heating body, the layers of the precursor are heat-fused. To produce a sheet. The molding conditions were as shown in Table 2. Then, the sheet was evaluated by the method described below.
  • a roll forming machine induction heating jacket roller manufactured by Tokuden Co., model JR-D0-W, roll diameter 200 mm ⁇ ⁇ 2 rolls, roll surface length 410 mm
  • Example 2 A sheet was produced and evaluated in the same manner as in Example 1 except that the biaxially stretched film C was used instead of the biaxially stretched film B.
  • Example 3 Ten biaxially stretched films AB were laminated and one biaxially stretched film A was laminated thereon to prepare a precursor in which both outermost layers were the biaxially stretched film A. A sheet was produced using the precursor in the same manner as in Example 1 and evaluated.
  • Example 4 A sheet was produced and evaluated in the same manner as in Example 3 except that the heating roll forming take-off speed was changed.
  • Example 5 A sheet was manufactured and evaluated in the same manner as in Example 3 except that the number of laminated biaxially stretched films was changed to a sheet thickness of 4 mm and the heating roll temperature was changed.
  • Example 6 to 11 A sheet was produced and evaluated in the same manner as in Example 3 except that the biaxially stretched film to be laminated was changed as shown in Table 2.
  • Example 12 A stack of 19 biaxially stretched films BAB and two biaxially stretched films A, one at each end, was laminated to prepare a precursor in which both outermost layers were biaxially stretched films A. A sheet was produced using the precursor in the same manner as in Example 1 and evaluated.
  • Comparative Example 1 Using only the biaxially stretched film A, a comparative sheet was manufactured and evaluated in the same manner as in Example 1.
  • Comparative Example 2 A comparative sheet was manufactured and evaluated in the same manner as in Comparative Example 1 except that the heating roll temperature was changed.
  • Example 3 A precursor was prepared using only the biaxially stretched film B. A comparative sheet was produced and evaluated in the same manner as in Example 1 using the precursor. However, the heating roll temperature was set as shown in Table 2.
  • Comparative Example 4 A comparative sheet was manufactured and evaluated in the same manner as in Comparative Example 3 except that the heating roll temperature was changed.
  • Comparative Example 8 A comparative sheet was manufactured and evaluated in the same manner as in Comparative Example 7 except that the heating roll temperature was changed.
  • Comparative Example 9 A comparative sheet was produced and evaluated in the same manner as in Example 1 except that the biaxially stretched film D was used instead of the biaxially stretched film B.
  • Comparative Example 10 A comparative sheet was produced and evaluated in the same manner as in Example 3 except that the biaxially stretched film AD was used instead of the biaxially stretched film AB-1.
  • Comparative Example 11 A comparative sheet was produced and evaluated in the same manner as in Comparative Example 10 except that the heating roll temperature was changed.
  • the resulting two-dimensional profile is, after removing the background, determine the integrated intensity I X V in azimuth of integrated intensity I X L and meridian (Z-axis) direction at the azimuth angle of the equatorial (Y-axis) direction It was The region of integration was the range from the equator (Y axis) and the meridian (Z axis) to the azimuth angle ⁇ 30 °.
  • the size of the X-ray incident beam at the sample irradiation position needs to be smaller than the thickness of the sheet in order to avoid the influence of reflection on the sheet surface. This time, the beam size at the sample irradiation position was set to 700 ⁇ m for a 1 mm thick sheet.
  • FIG. 1 shows an example of the laminated state a and the laminated state b. It can be seen that the dark portion in FIG. 1A is the second layer, and the layers between the first layer and the second layer are not separated.
  • FIG. 2B is a sheet composed of a plurality of first layers, and the dark dark portion indicates peeling.
  • the sheet obtained by the production method of the present invention has excellent transparency and mechanical properties.
  • a multilayer structure without any delamination could be observed.
  • Comparative Examples 9 and 10 partial peeling occurred due to the force applied during the slice slice by the microtome. It is considered that the tensile elastic modulus also has a low value obtained due to peeling during the measurement.
  • Comparative Examples 1, 3, 6, and 7, the slices could not be sliced well with the microtome because the layers were completely delaminated only by applying a slight force. It is considered that the value obtained due to peeling during the measurement of the tensile modulus decreased.
  • Comparative Examples 2, 4, 5, 8, and 11 since the film was melted by the stretching roll, a multilayer structure could not be confirmed in the obtained sheet.

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  • Engineering & Computer Science (AREA)
  • Mechanical Engineering (AREA)
  • Physics & Mathematics (AREA)
  • Thermal Sciences (AREA)
  • Laminated Bodies (AREA)
  • Shaping By String And By Release Of Stress In Plastics And The Like (AREA)
  • Lining Or Joining Of Plastics Or The Like (AREA)
PCT/JP2019/039822 2018-10-09 2019-10-09 ポリプロピレンシートの製造方法 Ceased WO2020075755A1 (ja)

Priority Applications (8)

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BR112021006684-5A BR112021006684B1 (pt) 2018-10-09 2019-10-09 Método para produzir chapa de polipropileno e método para produzir artigo conformado
EP19871892.6A EP3865285A4 (en) 2018-10-09 2019-10-09 POLYPROPYLENE SHEET PRODUCTION METHOD
MX2021004089A MX2021004089A (es) 2018-10-09 2019-10-09 Metodo de produccion de lamina de polipropileno.
JP2020551196A JP7279066B2 (ja) 2018-10-09 2019-10-09 ポリプロピレンシートの製造方法
US17/283,938 US12172359B2 (en) 2018-10-09 2019-10-09 Production method of polypropylene sheet
CN201980066336.9A CN112955308B (zh) 2018-10-09 2019-10-09 聚丙烯片材的制造方法
CA3115748A CA3115748C (en) 2018-10-09 2019-10-09 Production method of polypropylene sheet
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