Low-voc modified polypropylene composition, biaxially stretched polypropylene film and application and green and environment-friendly polypropylene capacitor film

Abstract

The application belongs to the field of polymers and relates to a low-VOC modified polypropylene composition, a biaxially stretched polypropylene film and a green and environment-friendly polypropylene capacitor film. The modified polypropylene composition comprises modified polypropylene grafted with an alkenyl functional monomer, a VOC inhibitor, an antioxidant and a processing aid. The modified polypropylene grafted with the alkenyl functional monomer comprises structural units derived from polypropylene as a matrix phase and structural units derived from the alkenyl functional monomer as a dispersed phase. The biaxially stretched polypropylene film of the application can maintain good dielectric properties and energy storage properties at a high working temperature and is suitable for high-temperature and high-operation-field-strength working conditions.

Description

Technical Field

[0001] This invention belongs to the field of polymers, specifically relating to a low-VOC modified polypropylene composition, a biaxially oriented polypropylene film made from the modified polypropylene composition, the application of the biaxially oriented polypropylene film in the preparation of energy storage dielectrics, and a green and environmentally friendly polypropylene capacitor film. Background Technology

[0002] Energy is the driving force of modern societal development. In recent years, with the rapid development of new energy, aerospace, underground resource extraction, and national defense industries, the demand for dielectric capacitors has increased year by year, and they are required to operate under more stringent temperature conditions. However, thin-film capacitors, primarily composed of polymer dielectric materials, have poor thermal stability and cannot operate stably in high-temperature environments. Especially under high electric fields, the temperature rise causes the leakage current inside the polymer dielectric to increase exponentially, resulting in a sharp decrease in charging and discharging efficiency and energy storage density, failing to meet application requirements. More seriously, the leakage current is converted into Joule heat, causing the capacitor temperature to rise continuously, ultimately leading to damage.

[0003] Biaxially oriented polypropylene (BOPP) is currently the most commercially available and widely used polymer film capacitor dielectric material. It has excellent comprehensive performance and mature large-scale preparation process, and is now widely used in industries such as electric vehicles, wind power, photovoltaics, lighting and railway locomotives.

[0004] However, an inherent drawback of polypropylene film capacitors is their poor dielectric energy storage performance and significantly reduced reliability at high temperatures. For example, at room temperature, BOPP can still achieve a charge-discharge efficiency of over 95% even when close to its breakdown field strength, but at 120°C, its efficiency drops to about 70%. This not only significantly reduces its energy storage density but also generates a large amount of waste heat that accumulates inside the device, ultimately leading to overheating and damage (thermal runaway).

[0005] Currently, there are two main types of methods to improve the operating temperature of polymer capacitor films from a materials perspective. The first type is to improve the thermal stability of the polymer dielectric material, that is, to synthesize materials with a high glass transition temperature (T0). g The first method involves polymer dielectric materials. The second method involves introducing a second-phase filler into the polymer dielectric material to prepare a composite material. This filler particles capture and scatter charge carriers to suppress leakage current in the polymer under high temperature and high electric field conditions. However, both methods suffer from complex manufacturing processes, making large-scale industrial production difficult.

[0006] Therefore, it is necessary to find a new type of modified polypropylene composition that has obvious controllability of dielectric energy storage characteristics, simple preparation process, and is suitable for practical engineering applications.

[0007] Grafting modification is a common method for functionalizing polypropylene. Commonly used methods include melt grafting and solid-phase grafting. Melt grafting equipment is simple and inexpensive, but the reaction temperature is high, the process is difficult to control, and there are many byproducts. It is also limited to a limited range of applicable monomers and is currently only used for the preparation of anhydride-based or a few acrylate-based compatibilizers. Solid-phase grafting occurs at temperatures below the melting point of polypropylene, resulting in fewer side reactions, higher grafting efficiency, and a wider range of applicable graft monomers. For example, Y. Pan et al. studied the reaction conditions for solid-phase grafting of glycidyl methacrylate (GMA) onto polypropylene in "Solid-phase grafting of glycidyl methacrylate onto polypropylene." (Journal of Applied Polymer Science, 1997, 65(10): 1905-1912), and pointed out that the influencing factors of solid-phase grafting and melt grafting are significantly different. Suspension grafting is a special type of solid-phase grafting. By introducing an aqueous medium as a dispersant into the reaction system, the reaction temperature is further reduced, improving the uniformity of grafting and reducing the formation of byproducts. In addition, Li Qiaojun et al. discussed the reaction conditions and influencing factors of polypropylene suspension grafting with styrene in "Study on polypropylene suspension grafting with styrene" (Synthetic Resins and Plastics, 1996, 13(1):7-10.). Zhu Baodong et al. reported that a polypropylene dimonomer graft with a grafting rate of 8.97% was obtained by aqueous suspension grafting in "Polypropylene aqueous suspension grafting with styrene and maleic anhydride" (Modern Plastics Processing and Application, 2009, 5:3.).

[0008] Most research on low-VOC polypropylene materials employs chemical reactions, physical adsorption, and melt devolatilization techniques to improve the VOC emission problem in existing polypropylene materials. Physical adsorption can adsorb all small molecules produced by PP, and adding physical adsorbents is a common method. For example, CN17273894 discloses the use of fine-porous silica gel and molecular sieves as adsorbents to reduce the odor and volatilization of organic compounds in materials. CN102276921A discloses the use of plant fibers as adsorbents to reduce the odor of polypropylene materials. While the aforementioned methods using adsorbents have some effect on reducing polypropylene VOCs, considering the application of polypropylene compositions in dielectric energy storage materials, it is necessary to consider the adsorption efficiency of physical adsorbents, their compatibility with polypropylene materials, and their impact on the dielectric properties of polypropylene materials. Therefore, researching new polypropylene dielectric material compositions with low-VOC characteristics is of great significance. Summary of the Invention

[0009] The purpose of this invention is to provide a low-VOC modified polypropylene composition containing a novel alkenyl functional monomer grafted modified polypropylene. High-performance low-VOC polypropylene films can be further prepared through a biaxial stretching process. The modified polypropylene composition and polypropylene films can maintain high energy storage efficiency and energy storage density even at high operating temperatures, and can be used as green and environmentally friendly capacitor films.

[0010] A first aspect of the present invention provides a low-VOC modified polypropylene composition comprising modified polypropylene grafted with an alkenyl functional monomer, a VOC inhibitor, an antioxidant, and a processing aid.

[0011] The modified polypropylene grafted with alkenyl functional monomers comprises structural units derived from polypropylene as the matrix phase and structural units derived from alkenyl functional monomers as the dispersed phase; the ash content of the modified polypropylene grafted with alkenyl functional monomers is less than 50 ppm, preferably less than 36 ppm, more preferably less than 30 ppm; the mass ratio of structural units derived from alkenyl functional monomers and in the grafted state to structural units derived from alkenyl functional monomers and in the self-polymerized state in the modified polypropylene grafted with alkenyl functional monomers is greater than or equal to 1.0, preferably 1.1 to 10, more preferably 1.2 to 6; the D50 of the dispersed phase is less than 450 nm, preferably 50 to 400 nm.

[0012] A second aspect of the present invention provides a biaxially oriented polypropylene film, which is prepared from the above-described low-VOC modified polypropylene composition.

[0013] A third aspect of the present invention provides the application of the above-described biaxially oriented polypropylene film in energy storage media, particularly high-temperature energy storage media.

[0014] A fourth aspect of the present invention provides a green and environmentally friendly polypropylene capacitor film, wherein the polypropylene capacitor film is one or more layers, wherein at least one layer is the above-mentioned biaxially oriented polypropylene film.

[0015] The modified polypropylene composition of this invention, as well as the biaxially oriented polypropylene film and polypropylene capacitor film made therefrom, have a wide operating temperature range. In particular, they maintain good dielectric and energy storage properties even at higher operating temperatures, making them especially suitable for high-temperature, high-field-strength operating conditions. Compared to inorganic filler doping technology, grafting modification can form a uniformly distributed nanoscale dispersed phase in the composite material, avoiding the problems of difficulty in adding and dispersing inorganic fillers. Compared to surface modification, bulk modification has a simpler process flow, produces a uniformly dispersed phase, and has a stable structure, making it less prone to functional monomer layer detachment due to external forces during use. Adding VOC inhibitors can further reduce the VOC content of the material. The biaxially oriented polypropylene film and high-performance polypropylene capacitor film of this invention have the advantages of good tensile properties, environmental friendliness, and low odor. They can balance mechanical and electrical properties at higher operating temperatures, making them suitable for high-temperature, high-field-strength operating conditions.

[0016] Other features and advantages of the present invention will be described in detail in the following detailed description section. Attached Figure Description

[0017] Exemplary embodiments of the present invention will be described in more detail with reference to the accompanying drawings.

[0018] Figure 1 The image shows the microstructure of the modified polypropylene sample from Example 1 under a 20,000x electron microscope, where the spherical dispersed phase is an aggregate of styrene structural units.

[0019] Figure 2 This is a microscopic image of the modified polypropylene sample from Example 2 under a 20,000x electron microscope.

[0020] Figure 3 This is a microscopic image of the modified polypropylene sample from Example 3 under a 20,000x electron microscope.

[0021] Figure 4 This is a microscopic image of the modified polypropylene sample from Example 10 under a 20,000x electron microscope.

[0022] Figure 5 The image shows the microstructure of the modified polypropylene sample in Comparative Example 1 under a 20,000x electron microscope, with no visible dispersed phase. Detailed Implementation

[0023] The following provides a detailed description of specific embodiments of the present invention. It should be understood that the specific embodiments described herein are for illustrative and explanatory purposes only and are not intended to limit the scope of the invention.

[0024] This invention provides a low-VOC modified polypropylene composition comprising modified polypropylene grafted with alkenyl functional monomers, a VOC inhibitor, an antioxidant, and a processing aid.

[0025] The modified polypropylene grafted with alkenyl functional monomers comprises structural units derived from polypropylene as the matrix phase and structural units derived from alkenyl functional monomers as the dispersed phase; the ash content of the modified polypropylene grafted with alkenyl functional monomers is less than 50 ppm, preferably less than 36 ppm, more preferably less than 30 ppm; the mass ratio of structural units derived from alkenyl functional monomers and in the grafted state to structural units derived from alkenyl functional monomers and in the self-polymerized state in the modified polypropylene grafted with alkenyl functional monomers is greater than or equal to 1.0, preferably 1.1 to 10, more preferably 1.2 to 6; the D50 of the dispersed phase is less than 450 nm, preferably 50 to 400 nm.

[0026] According to the present invention, preferably, the modified polypropylene grafted with the alkenyl functional monomer has at least one of the following characteristics: a melt flow rate of 1–10 g / 10 min at 230°C and a load of 2.16 kg, preferably 1.5–8 g / 10 min, more preferably 2–5 g / 10 min. Melting temperature T m The temperature range is 155–168℃, preferably 157–165℃. The flexural modulus is 1400–2000 MPa, preferably 1500–1800 MPa.

[0027] In this invention, the term "structural unit" refers to a portion of modified polypropylene grafted with an alkenyl functional monomer, and its form is not limited. Specifically, "structural unit derived from polypropylene" refers to a product formed from polypropylene, which includes both "group" and "polymer" forms. "Structural unit derived from alkenyl functional monomer" refers to a product formed from an alkenyl functional monomer, which includes both "group" and "self-polymerized" forms. The "structural unit" can be a repeating unit or a non-repeating independent unit. A structural unit derived from an alkenyl functional monomer in a "grafted state" refers to a structural unit derived from an alkenyl functional monomer that has formed a covalent bond (graft) with polypropylene.

[0028] Specifically, the modified polypropylene grafted with alkenyl functional monomers has a "sea-island structure," such as... Figure 1 As shown. The "sea" phase is the matrix phase, formed from structural units derived from polypropylene. The "island" phase is the dispersed phase, formed from structural units derived from alkenyl functional monomers.

[0029] According to the present invention, preferably, the modified polypropylene grafted with the alkenyl functional monomer is prepared by a grafting reaction of polypropylene and the alkenyl functional monomer, more preferably by a suspension grafting reaction. The grafting reaction of the present invention is a free radical polymerization reaction; therefore, "in the grafted state" refers to the state in which the monomer, after free radical polymerization, forms a bond with another reactant. "The self-polymerized state" refers to the state in which the monomer forms a self-polymer and is not bonded (grafted) to another reactant. The bond includes both direct and indirect bonds.

[0030] According to the present invention, preferably, the modified polypropylene grafted with alkenyl functional monomers has at least one of the following characteristics:

[0031] - Maximum operating temperature ≥100℃, preferably 110~160℃, more preferably 120~145℃;

[0032] The breakdown field strength at -120℃ is Eg≥510MV / m, preferably 550~800MV / m;

[0033] DC volume resistivity ρ at -120℃ and 200MV / m electric field strength vg ≥6.0×10 13 Ω·m, preferably 1.0 × 10 14 Ω·m~1.0×10 20 Ω·m;

[0034] The dielectric constant at -120℃ and 100Hz is greater than 2.25, preferably 2.26 to 2.65;

[0035] The dielectric loss at -120℃ and 100Hz is less than 1.5E-3, preferably 1.0E-6 to 1.3E-3;

[0036] The energy storage density at -120℃ and 300MV / m is greater than 0.720J / cm³. 3 The preferred value is 0.740–2.0 J / cm³. 3 ;

[0037] The energy storage efficiency at -120℃ and 300MV / m is greater than 90.0%, preferably 92.0% to 99.0%.

[0038] The aforementioned properties of the modified polypropylene grafted with alkenyl functional monomers described in this invention were measured by fabricating it into a thin film.

[0039] The alkenyl group in the alkenyl-containing functional monomer of the present invention is used for grafting with polypropylene. Therefore, any alkenyl-containing functional monomer with the alkenyl group located in a reactive position is applicable to the present invention.

[0040] Specifically, the alkenyl-containing functional monomer is selected from at least one monomer having the structure shown in Formula 1.

[0041]

[0042] In Equation 1, R b R c R d Each is independently selected from H, substituted or unsubstituted alkyl groups; R a Selected from substituted or unsubstituted alkyl groups, substituted or unsubstituted alkoxy groups, substituted or unsubstituted aryl groups, substituted or unsubstituted ester groups, substituted or unsubstituted carboxyl groups, substituted or unsubstituted cycloalkyl or heterocyclic groups, cyano groups, and substituted or unsubstituted silyl groups; R a and R d Arrange the rings arbitrarily.

[0043] According to a preferred embodiment of the present invention, R b R c R d Each is independently selected from H, substituted or unsubstituted C1-C6 alkyl groups; R a Selected from substituted or unsubstituted C1-C 20 Alkyl, substituted or unsubstituted C1-C 20 Alkoxy, substituted or unsubstituted C6-C 20 aryl, substituted or unsubstituted C1-C 20 Ester group, substituted or unsubstituted C1-C 20 Carboxyl, substituted or unsubstituted C3-C 20 Cycloalkyl or heterocyclic, cyano, substituted or unsubstituted C3-C 20 Silyl group; the substituted group is halogen, -OH, -NH2, =O, C1-C 12 Alkyl, C3-C6 cycloalkyl, C1-C 12 alkoxy groups, C1-C 12 Acyloxy group; R a and R d Optionally, it can form a 4-6 membered heterocycle with a double bond.

[0044] According to a more preferred embodiment of the present invention, wherein R b R c R d Each is independently selected from H, substituted or unsubstituted C1-C6 alkyl groups;

[0045] R a It is selected from at least one of the groups shown in Formula 2, Formula 3, Formula 4, Formula 5, Formula 6, and heterocyclic groups;

[0046]

[0047] In Equation 2, R 4 -R 8 Each is independently selected from H, halogen, hydroxyl, amino, phosphate group, sulfonic acid group, substituted or unsubstituted C1-C. 12 Alkyl, substituted or unsubstituted C3-C 12 cycloalkyl, substituted or unsubstituted C1-C 12 alkoxy, substituted or unsubstituted C1-C 12 ester group, substituted or unsubstituted C1-C 12 The substituted amino group, wherein the substituted group is selected from halogen, hydroxyl, amino, phosphate, sulfonic acid, C1-C 12 Alkyl, C3-C 12 cycloalkyl, C1-C 12 alkoxy groups, C1-C 12 ester group, C1-C 12 The amino group; preferably, R 4 -R 8 Each is independently selected from H, halogen, hydroxyl, amino, substituted or unsubstituted C1-C6 alkyl, substituted or unsubstituted C1-C6 alkoxy;

[0048]

[0049] In Equation 3, R4-R 10 Each is independently selected from H, halogen, hydroxyl, amino, phosphate group, sulfonic acid group, substituted or unsubstituted C1-C. 12 Alkyl, substituted or unsubstituted C3-C 12 cycloalkyl, substituted or unsubstituted C1-C 12 alkoxy, substituted or unsubstituted C1-C 12 ester group, substituted or unsubstituted C1-C 12 The substituted amino group, wherein the substituted group is selected from halogen, hydroxyl, amino, phosphate, sulfonic acid, C1-C 12 Alkyl, C3-C 12 cycloalkyl, C1-C 12 alkoxy groups, C1-C 12 ester group, C1-C 12 The amino group; preferably, R4-R 10 Each of the groups is independently selected from H, halogen, hydroxyl, amino, substituted or unsubstituted C1-C6 alkyl, substituted or unsubstituted C1-C6 alkoxy, wherein the substituted group is selected from halogen, hydroxyl, amino, C1-C6 alkyl, C1-C6 alkoxy;

[0050]

[0051] In Equation 4, R4'-R 10 Each group is independently selected from H, halogen, hydroxyl, amino, phosphate, sulfonic acid, substituted or unsubstituted C1-C. 12 Alkyl, substituted or unsubstituted C3-C 12 cycloalkyl, substituted or unsubstituted C1-C 12 alkoxy, substituted or unsubstituted C1-C 12 ester group, substituted or unsubstituted C1-C 12 The substituted amino group, wherein the substituted group is selected from halogen, hydroxyl, amino, phosphate, sulfonic acid, C1-C 12 Alkyl, C3-C 12 cycloalkyl, C1-C 12 alkoxy groups, C1-C 12 ester group, C1-C 12 The amino group; preferably, R4'-R 10 Each of the following is independently selected from H, halogen, hydroxyl, amino, substituted or unsubstituted C1-C6 alkyl, substituted or unsubstituted C1-C6 alkoxy, wherein the substituted group is selected from halogen, hydroxyl, amino, C1-C6 alkyl, C1-C6 alkoxy;

[0052]

[0053] In Equation 5, R', R”, and R”' are each independently selected from substituted or unsubstituted C1-C. 12 Straight-chain alkyl, substituted or unsubstituted C3-C 12 Branched alkyl, substituted or unsubstituted C1-C 12 alkoxy, substituted or unsubstituted C1-C 12 The acyloxy group; preferably, R1 is a C2-C6 alkenyl group, preferably a monounsaturated alkenyl group; R2, R3, and R4 are each independently selected from substituted or unsubstituted C1-C6 straight-chain alkyl groups, substituted or unsubstituted C3-C6 branched alkyl groups, substituted or unsubstituted C1-C6 alkoxy groups, and substituted or unsubstituted C1-C6 acyloxy groups;

[0054]

[0055] In Equation 6, R m Selected from hydroxyl groups and / or substituted or unsubstituted groups: C1-C 20 Straight-chain alkyl, C3-C 20 Branched alkyl, C3-C 12 cycloalkyl, C3-C 12 Epoxyalkyl, C3-C 12 Epoxyalkylalkyl, wherein the substituted group is selected from at least one of halogen, amino and hydroxyl groups;

[0056] The heterocyclic group is selected from imidazole, pyrazol, carbazole, pyrrolidone, pyridinyl, piperidinyl, caprolactam, pyrazinyl, thiazolyl, purine, morpholino, and oxazolino.

[0057] According to a specific embodiment of the present invention, the alkenyl-containing functional monomer is a styrene monomer, wherein the styrene monomer is selected from at least one of styrene, α-methylstyrene, 1-vinylnaphthalene, 2-vinylnaphthalene, monosubstituted or polysubstituted styrene, monosubstituted or polysubstituted α-methylstyrene, monosubstituted or polysubstituted 1-vinylnaphthalene, and monosubstituted or polysubstituted 2-vinylnaphthalene; the substituted group is preferably selected from at least one of halogen, hydroxyl, amino, phosphate group, sulfonic acid group, C1-C8 straight-chain alkyl, C3-C8 branched alkyl or cycloalkyl, C1-C6 straight-chain alkoxy, C3-C8 branched alkoxy or cyclic alkoxy, C1-C8 straight-chain ester group, C3-C8 branched ester group or cyclic ester group, C1-C8 straight-chain amino group, and C3-C8 branched amino group or cyclic amino group; preferably, the styrene monomer is selected from at least one of styrene, α-methylstyrene, 2-methylstyrene, 3-methylstyrene, and 4-methylstyrene.

[0058] According to a specific embodiment of the present invention, the alkenyl-containing functional monomer is an alkenyl-containing silane monomer, wherein the alkenyl-containing silane monomer is selected from at least one of vinyltriethoxysilane, vinyltrimethoxysilane, vinyltriisopropoxysilane, vinyltritert-butoxysilane, vinyltriacetoxysilane, methylvinyldimethoxysilane, ethylvinyldiethoxysilane, allyltriethoxysilane, allyltrimethoxysilane, allyltriisopropoxysilane, vinyltris(β-methoxyethoxy)silane, allyltris(β-methoxyethoxy)silane, allyltritert-butoxysilane, allyltriacetoxysilane, methylallyldimethoxysilane, and ethylallyldiethoxysilane.

[0059] According to one specific embodiment of the present invention, the alkenyl-containing functional monomer is an acrylate monomer and / or an acrylic monomer. Preferably, the acrylate monomer is selected from at least one of methyl methacrylate, sec-butyl methacrylate, ethyl methacrylate, n-butyl methacrylate, isobutyl methacrylate, tert-butyl methacrylate, isooctyl methacrylate, dodecyl methacrylate, coconut oleate methacrylate, octadecyl methacrylate, dimethylaminoethyl methacrylate, diethylaminoethyl methacrylate, dimethylaminopropyl methacrylate, and glycidyl methacrylate. Preferably, the acrylic monomer is selected from at least one of acrylic acid, methacrylic acid, and 2-ethylacrylic acid.

[0060] In this invention, C3-C 12 Epoxyalkyl refers to an alkyl group that has 3-12 carbon atoms and is substituted with an epoxyalkyl group, such as ethylene oxide methyl.

[0061] According to a specific embodiment of the present invention, the alkenyl-containing functional monomer is an alkenyl-containing heterocyclic compound. The alkenyl-containing heterocyclic monomer of the present invention can be any alkenyl-containing heterocyclic compound capable of free radical polymerization, and can be selected from at least one of the following: imidazoles containing alkenyl substituents, pyrazoles containing alkenyl substituents, carbazoles containing alkenyl substituents, pyrrolidones containing alkenyl substituents, pyridines or pyridine salts containing alkenyl substituents, piperidines containing alkenyl substituents, caprolactams containing alkenyl substituents, pyrazines containing alkenyl substituents, thiazoles containing alkenyl substituents, purines containing alkenyl substituents, morpholines containing alkenyl substituents, and oxazolines containing alkenyl substituents; preferably, the alkenyl-containing heterocyclic monomer is a monoalkenyl-containing heterocyclic monomer.

[0062] Specifically, the alkenyl-containing heterocyclic monomer may be selected from at least one of the following: 1-vinylimidazolium, 2-methyl-1-vinylimidazolium, N-allylimidazolium, 1-vinylpyrazole, 3-methyl-1-vinylpyrazole, vinylcarbazole, N-vinylpyrrolidone, 2-vinylpyridine, 3-vinylpyridine, 4-vinylpyridine, 2-methyl-5-vinylpyridine, vinylpyridine N-oxide, vinylpyridine salt, vinylpiperidine, N-vinylcaprolactam, 2-vinylpyrazine, N-vinylpiperazine, 4-methyl-5-vinylthiazole, N-vinylpurine, vinylmorpholine, and vinyloxazoline.

[0063] According to the present invention, the alkenyl-containing functional monomer may further be at least one selected from maleic anhydride, maleimide and its derivatives, itaconic anhydride, and α-methylene-γ-butyrolactone. Preferably, the alkenyl-containing functional monomer is maleic anhydride.

[0064] In this invention, various types of alkenyl-containing functional monomers can be used alone or in combination with one or more.

[0065] The polypropylene mentioned in this invention refers to the polypropylene portion of the grafted material, or it can refer to ungrafted polypropylene, which can be a propylene homopolymer or a propylene copolymer containing ethylene or butene units. More preferably, the polypropylene powder is a homopolymer polypropylene with an isotacticity greater than 96%, more preferably greater than 96.5%; or a copolymer polypropylene with a total content of ethylene and butene units of less than 3.0 mol% based on the total molar amount of structural units, for example, 2.5 mol%, 2 mol%, 1.5 mol%, 1 mol%, 0.9 mol%, 0.8 mol%, 0.7 mol%, 0.6 mol%, 0.5 mol%, 0.4 mol%, 0.3 mol%, 0.2 mol%, or 0.1 mol%. Preferably, the total content of ethylene and butene units in the copolymer polypropylene is greater than 0 and less than 0.1 mol%, or greater than 0.1 mol% and less than or equal to 3.0 mol%.

[0066] According to the present invention, in order to obtain the modified polypropylene grafted with alkenyl functional monomers with the aforementioned characteristics, it is preferable to use polypropylene having the following characteristics: particle size of 16 to 50 mesh; ash content of less than 55 ppm, preferably less than 40 ppm, more preferably less than 35 ppm; and flexural modulus of 1400 to 2000 MPa, preferably 1500 to 1800 MPa.

[0067] In addition to the above-mentioned features, the polypropylene preferably also has at least one of the following features: a melt flow rate of 0.5 to 10 g / 10 min at 230°C and 2.16 kg load, preferably 1 to 5 g / 10 min, more preferably 2 to 4 g / 10 min; and / or a melt temperature Tm of 150°C or higher, preferably 153 to 180°C, more preferably 155 to 167°C.

[0068] The polypropylene powder suitable for this invention is commercially available or can be prepared by the methods described in Chinese patents CN109694427A, CN109694428A, CN104558813A, CN109912734A, CN111019025A, and CN105431459A.

[0069] The modified polypropylene grafted with alkenyl functional monomers of the present invention can be prepared by a method comprising the following steps: in the presence of an inert gas, a reaction mixture comprising polypropylene and alkenyl functional monomers is subjected to a grafting reaction to obtain the modified polypropylene grafted with alkenyl functional monomers.

[0070] The grafting reaction of this invention can be carried out with reference to various methods conventional in the art, preferably a suspension grafting reaction. For example, active grafting sites are formed on polypropylene in the presence of an alkenyl-containing functional monomer for grafting, or active grafting sites are first formed on polypropylene and then treated with a grafting monomer. Grafting sites can be formed by treatment with a free radical initiator, or by high-energy ionizing radiation or microwave treatment. Free radicals generated in the polymer as a result of chemical or radiation treatment form grafting sites on the polymer and initiate monomer polymerization at these sites.

[0071] Preferably, the grafting site is initiated by a free radical initiator and a grafting reaction is further carried out. In this case, the reaction mixture further includes a free radical initiator; more preferably, the free radical initiator is selected from peroxide free radical initiators and / or azo free radical initiators.

[0072] The peroxide radical initiator is preferably selected from at least one of benzoyl peroxide, dicumyl peroxide, di-tert-butyl peroxide, lauroyl peroxide, dodecyl peroxide, tert-butyl peroxide, diisopropyl peroxide, tert-butyl peroxide, and dicyclohexyl peroxide; the azo radical initiator is preferably azobisisobutyronitrile and / or azobisisoheptanenitrile.

[0073] More preferably, the grafting site is initiated by a peroxide-based free radical initiator and the grafting reaction is further carried out.

[0074] Furthermore, the grafting reaction of the present invention can also be carried out by the methods described in CN106543369A, CN104499281A, CN102108112A, CN109251270A, CN1884326A and CN101492517B.

[0075] Provided that the above-mentioned product characteristics are met, the present invention does not impose any particular limitation on the amount of each component used in the grafting reaction. Specifically, the mass ratio of the free radical initiator to the alkenyl-containing functional monomer can be 0.1 to 10:100, preferably 0.5 to 5:100. The mass ratio of the alkenyl-containing functional monomer to the polypropylene can be 0.5 to 25:100, preferably 1 to 20:100.

[0076] The present invention does not particularly limit the process conditions for the grafting reaction. Specifically, the temperature of the grafting reaction can be 30-110°C, preferably 60-95°C; the time can be 0.5-10h, preferably 1-6h.

[0077] In this invention, the "reaction mixture" includes all materials added to the grafting reaction system. The materials can be added all at once or at different stages of the reaction.

[0078] The reaction mixture of the present invention also includes deionized water as a dispersant. The amount of deionized water is 300-800% of the total mass of the polypropylene powder and the alkenyl-containing functional monomer.

[0079] The reaction mixture of the present invention may further include an organic solvent as a solvent for dissolving the solid free radical initiator. The organic solvent preferably includes at least one of C2-C5 alcohols, C2-C4 ethers, and C3-C5 ketones; more preferably, it includes at least one of C2-C4 alcohols, C2-C3 ethers, and C3-C5 ketones; and most preferably, it includes at least one of ethanol, diethyl ether, and acetone. The mass content of the organic solvent is preferably 1-35% of the mass of the polypropylene powder.

[0080] According to the present invention, the preparation method of the modified polypropylene grafted with the alkenyl functional monomer can be selected from one of the following methods:

[0081] Method 1, the preparation method includes the following steps:

[0082] a. Place the polypropylene powder in a closed reactor and replace it with an inert gas;

[0083] b. Add the free radical initiator and the alkenyl-containing functional monomer to the closed reactor and stir to mix;

[0084] c. Add deionized water to raise the temperature of the reaction system to the grafting reaction temperature and carry out the grafting reaction; optionally, allow the reaction system to swell before or after adding deionized water;

[0085] d. After the reaction is complete, the mixture is filtered and dried to obtain the modified polypropylene grafted with the alkenyl functional monomer.

[0086] Method 2, the preparation method includes the following steps:

[0087] a. Place the polypropylene powder in a closed reactor and replace it with an inert gas;

[0088] b. Mix the organic solvent and the free radical initiator, and add them to the closed reactor;

[0089] c. Remove the organic solvent, add an alkenyl-containing functional monomer, and optionally swell the reaction system;

[0090] d. Add deionized water to raise the temperature of the reaction system to the grafting reaction temperature and carry out the grafting reaction;

[0091] e. After the reaction is complete, the mixture is filtered and dried to obtain the modified polypropylene grafted with the alkenyl functional monomer.

[0092] According to the method of the present invention, the polypropylene powder used can be commercially available as a product with a suitable particle size, or it can be purchased or made in-house and then screened. Therefore, the present invention may also include a step of screening pretreatment of the polypropylene powder. Screening can be achieved using conventional sieving methods. According to a preferred embodiment, the screening pretreatment includes the following steps: screening the powder using a double-layer vibrating screen or linear screen equipped with a screen of appropriate mesh size, and using the polypropylene powder in the middle layer of the screening machine as the reactant to obtain raw material powder with a corresponding particle size range.

[0093] According to a more specific embodiment of the present invention, the method for preparing the modified polypropylene grafted with the alkenyl functional monomer is selected from one of the following methods:

[0094] Method 1, the preparation method includes the following steps:

[0095] a. Use a double-layer vibrating screen or linear screen equipped with 16-mesh and 48-mesh screens to screen the powder, and use the polypropylene powder in the middle layer of the screening machine as the reaction material.

[0096] b. Place the polypropylene powder in the middle layer of the screening machine into a closed reactor for inert gas replacement;

[0097] c. Dissolve the free radical initiator in an alkenyl functional monomer to prepare a solution, add it to a closed reactor containing polypropylene, and stir to mix.

[0098] d. Add deionized water, heat the system to the graft polymerization temperature of 30-110°C, and react for 0.5-10 hours; optionally, allow the reaction system to swell before or after adding deionized water;

[0099] e. After the reaction is complete, the mixture is filtered and dried to obtain the modified polypropylene grafted with the alkenyl functional monomer.

[0100] Method 2, the preparation method includes the following steps:

[0101] a. Use a double-layer vibrating screen or linear screen equipped with 16-mesh and 48-mesh screens to screen the powder, and use the polypropylene powder in the middle layer of the screening machine as the reaction material.

[0102] b. Place the polypropylene powder in the middle layer of the screening machine into a closed reactor for inert gas replacement;

[0103] c. Mix the organic solvent and the free radical initiator, and add them to the closed reactor;

[0104] c. Remove the organic solvent, add an alkenyl-containing functional monomer, and optionally swell the reaction system;

[0105] d. Add deionized water, heat the system to the graft polymerization temperature of 30-110℃, and react for 0.5-10 hours;

[0106] e. After the reaction is complete, the mixture is filtered and dried to obtain the modified polypropylene grafted with the alkenyl functional monomer.

[0107] The inert gas described in this invention can be any of the inert gases commonly used in the art, including but not limited to nitrogen and argon.

[0108] According to the present invention, based on 100 parts by weight of modified polypropylene, the content of the VOC inhibitor can be 0.1 to 3 parts by weight, preferably 0.5 to 2 parts by weight.

[0109] According to a preferred embodiment of the present invention, the VOC inhibitor comprises the following components: fully vulcanized powdered silicone rubber, zeolite powder, and boehmite; wherein, based on the total weight of the VOC inhibitor, the content of fully vulcanized powdered silicone rubber is 8 wt% to 70 wt%, preferably 50 wt% to 70 wt%; the content of zeolite powder is 10 wt% to 65 wt%, preferably 15 wt% to 40 wt%; and the content of boehmite is 5 wt% to 40 wt%, preferably 6 wt% to 25 wt%.

[0110] According to some embodiments of the present invention, the fully vulcanized powdered silicone rubber has an average particle size of 0.05–1 μm, preferably 0.05–0.2 μm, more preferably 0.05–0.1 μm; the rubber particles have a cross-linked structure, and the gel content is 60 wt% or higher, preferably 75 wt% or higher, more preferably 90 wt% or higher. The fully vulcanized powdered silicone rubber particles preferably have a homogeneous structure, meaning that each particle in the fully vulcanized powdered silicone rubber is homogeneous, and each individual particle is homogeneous in composition. No heterogeneous phenomena such as layering or phase separation are found within the particles under existing microscopic observation techniques. The particle size of this powdered rubber is fixed by cross-linking the corresponding rubber latex through irradiation. For detailed information on the fully vulcanized powdered silicone rubber and its preparation method, please refer to Chinese Patent CN1383439A, the entire contents of which are incorporated herein by reference.

[0111] According to some embodiments of the present invention, the specific surface area of ​​the zeolite powder is 100-400 m². 2 / gr, preferably 150-300m 2 / gr.

[0112] According to some embodiments of the present invention, the average pore size of the zeolite powder is 0.1-20 nm, preferably 0.3-15 nm; the fineness is 1000-2500 mesh, preferably 1200-2500 mesh.

[0113] According to some embodiments of the present invention, the specific surface area of ​​the pseudoboehmite is 100–350 m². 2 / gr, preferably 200-320m 2 / gr.

[0114] According to some embodiments of the present invention, the average pore size of the pseudoboehmite is 2-60 nm, preferably 5-50 nm.

[0115] A compound of fully vulcanized powdered silicone rubber, zeolite powder, and boehmite can effectively adsorb different types of VOCs remaining in polypropylene, reducing the VOC release rate and delaying or preventing VOC emissions from polypropylene. The blending of these three components effectively improves the dispersion of nano-sized particles in polypropylene resin, enhances the adsorption efficiency of zeolite powder and boehmite, and significantly reduces the VOC release content in polypropylene. The fully vulcanized powdered silicone rubber itself, when nano-dispersed in polypropylene resin, can also adsorb residual VOCs to a certain extent, delaying their release. Furthermore, the nano-sized particles and their uniform dispersion in the polypropylene composition also play a positive role in improving the electrical insulation properties of the material, effectively inhibiting space charge accumulation.

[0116] The antioxidants described in this invention can be various antioxidants conventional in the art, such as one or more combinations selected from hindered phenols, hindered amines, phosphites, thiolated compounds, and benzofuranones. Specifically, the antioxidant is selected from at least one of pentaerythritol tetrakis[β-(3,5-di-tert-butyl-4-hydroxyphenyl)propionate] (antioxidant 1010), tris[2,4-di-tert-butylphenyl] phosphite (antioxidant 168), octadecyl β-(3,5-di-tert-butyl-4-hydroxyphenyl)propionate (antioxidant 1076), 2,2'-thiobis[3-(3,5-di-tert-butyl-4-hydroxyphenyl)propionate] (antioxidant 1035), 2,2'-methylenebis(4-methyl-6-tert-butylphenol) (antioxidant 2246), 1,1,3-tris(2-methyl-4-hydroxy-5-tert-butylphenyl)butane (antioxidant CA), and bis(2,4-di-tert-butylphenol) pentaerythritol diphosphite (antioxidant 626). Based on 100 parts by weight of modified polypropylene, the content of antioxidant can be 0.1 to 0.8 parts by weight, preferably 0.1 to 0.5 parts by weight.

[0117] According to the present invention, the processing aids include, but are not limited to, lubricants, acid absorbers, slip agents, antistatic agents, and anti-sticking agents. The amounts of each aid can be conventionally selected in the art, as those skilled in the art will know, and will not be elaborated upon here. The processing aids used will not adversely affect the stretching film-forming properties or mechanical properties of the modified polypropylene composition. Based on 100 parts by weight of modified polypropylene, the content of the processing aid can be 0.05 to 1 part by weight, preferably 0.05 to 0.5 parts by weight.

[0118] According to some embodiments of the present invention, the processing aid is a lubricant. The lubricant may be selected from one or more of the following: polyethylene glycol lubricants, fluoropolymer lubricants, silicone lubricants, fatty alcohol lubricants, fatty acid lubricants, fatty acid ester lubricants, stearamide lubricants, fatty acid metal soap lubricants, alkane and oxidized alkane lubricants, and micro / nano particle lubricants.

[0119] Specifically, the PEG-based lubricant can be, for example, a PEG molecule with a molecular weight of 500 to 50,000, which can be end-capped, grafted, cross-linked, or subjected to other chemical or physical modifications. The fluoropolymer lubricant can be, for example, at least one of polytetrafluoroethylene, polyvinylidene fluoride, and polyhexafluoropropylene, or other unimodal or multimodal fluoropolymers, as well as crystalline or semi-crystalline fluoropolymers. The silicone lubricant can be any existing compound with carbon or silicon atoms as the main molecular chain and oligomers or oligomers with organic groups such as methyl, phenyl, alkoxy, and vinyl as side chains. The fatty alcohol lubricant can be, for example, at least one of soft fatty alcohol, stearic alcohol, and tallow fatty alcohol. The fatty acid lubricant can be, for example, stearic acid and / or 12-hydroxystearic acid. The fatty acid ester lubricant can be, for example, at least one of butyl stearate, glyceryl monostearate, hexadecyl palmitate, and octadecyl stearate. The stearamide lubricant may be at least one of stearamide, oleamide, erucamide, n,n-ethylene bis-stearamide (EBS), etc. The fatty acid metal soap lubricant may be at least one of lead stearate, calcium stearate, magnesium stearate, synthetic calcium acetate, etc. The alkane and alkane oxide lubricant may be at least one of liquid paraffin, solid paraffin, polyethylene wax, polypropylene wax, ethylene oxide wax, etc. The micro / nano particle lubricant may be, for example, powdered rubber and / or silica gel microparticles.

[0120] According to a specific embodiment of the present invention, the processing aid is a fluoropolymer.

[0121] All of the above processing aids are commercially available.

[0122] The modified polypropylene composition of the present invention is prepared by mixing the components.

[0123] The present invention also provides a biaxially oriented polypropylene film, which is prepared from the above-described low-VOC modified polypropylene composition.

[0124] The method for forming polymer films from the modified polypropylene composition granules of the present invention can be carried out with reference to the prior art. For example, the granules can be processed by hot pressing or extrusion casting, or by biaxial stretching, to form a film.

[0125] According to a specific embodiment of the present invention, the biaxially oriented polypropylene film is prepared by a method comprising the following steps:

[0126] (1) The low-VOC modified polypropylene composition is mixed and granulated;

[0127] (2) The obtained granules are melt-extruded and cast into sheets to obtain modified polypropylene sheets;

[0128] (3) The modified polypropylene casting is biaxially stretched to obtain the biaxially stretched polypropylene film.

[0129] The process of mixing and extruding granules the modified polypropylene with VOC inhibitors, antioxidants, and processing aids in step (1) typically includes: mixing the modified polypropylene composition uniformly in a high-speed mixer; adding the uniformly mixed material to a twin-screw extruder or a single-screw extruder for melt mixing and uniform extrusion granulation; and drying to obtain granules. The processing temperature of the twin-screw extruder can be controlled between 190 and 230°C.

[0130] According to the present invention, the temperature of the melt extrusion in step (2) is 190-230°C; the temperature of the casting quench roll of the cast sheet is 15-50°C. The modified polypropylene cast sheet may be a single-layer structure or a multi-layer structure.

[0131] According to the present invention, preferably, the biaxially oriented polypropylene film has a longitudinal tensile strength ≥130 MPa, more preferably 140-170 MPa; a transverse tensile strength ≥190 MPa, more preferably 200-250 MPa; a longitudinal elongation at break ≥210%, more preferably 225-280%; a transverse elongation at break ≥60%, more preferably 62-90%; a VOC content of less than 50 μgC / g, more preferably less than 45 μgC / g, more preferably less than 42 μgC / g; and a thickness of 0.5-15 micrometers, more preferably 4-10 micrometers.

[0132] The biaxially oriented polypropylene film of this invention can be used as an energy storage dielectric, and is particularly suitable as a high-temperature energy storage dielectric due to its high operating temperature. The dielectric is preferably a membrane dielectric, which can be single-layer or multi-layered, including but not limited to capacitor films, roughened films, supercapacitor films, electrostatic films, or battery separators. The biaxially oriented polypropylene film of this invention is particularly suitable for preparing films for use in membrane capacitors, and can be directly applied as a polypropylene capacitor film, or used to prepare polypropylene capacitor films.

[0133] In this invention, the term "capacitor film," also known as capacitor film or electrical film, has a meaning that is well known in the art.

[0134] Specifically, the present invention provides a green and environmentally friendly polypropylene capacitor film, wherein the polypropylene capacitor film may be one or more layers, and at least one layer of the polypropylene capacitor film is the biaxially oriented polypropylene film.

[0135] The preparation of polypropylene capacitor film specifically includes: adding the modified polypropylene composition granules obtained in step (1) into a casting equipment for extrusion casting, and then stretching the resulting casting in a film biaxial stretching equipment. During the extrusion casting process, the casting die can be selected according to the desired film structure. For example, when a film with a single-layer structure is required, a single-layer die can be used; when a film with a multi-layer structure is required (e.g., a film with a three-layer structure of upper surface layer, core layer, and lower surface layer), a multi-layer composite die can be used, and at least one layer (e.g., the core layer) of the multi-layer composite die is connected to the extruder hopper containing the modified polypropylene composition, so that at least one layer (e.g., the core layer) of the resulting film is a modified polypropylene layer formed by the modified polypropylene composition. During the extrusion process, the extrusion temperature can be 100-200℃, and the temperature of the casting quenching roller can be 15-50℃.

[0136] In this invention, the biaxial stretching includes simultaneous stretching (i.e., simultaneous longitudinal (MD) and transverse (TD) stretching of the film) or step-by-step stretching (i.e., first longitudinal stretching of the film, then transverse stretching of the film).

[0137] The simultaneous stretching method includes: first, preheating the modified polypropylene composition casting sheet at a temperature of 120–170°C, and then simultaneously performing MD and TD stretching; the conditions for the simultaneous stretching method include: stretching temperature of 150–175°C, MD stretching ratio of more than 3 times, TD stretching ratio of more than 3 times, MD stretching rate of 50–300% / s, and TD stretching rate of 50–300% / s.

[0138] The stepwise stretching method includes: first preheating the modified polypropylene composition casting sheet, then performing MD stretching, then preheating again and then performing TD stretching; the conditions for the stepwise stretching method include: MD stretching temperature of 155-175℃, TD stretching temperature of 155-175℃, MD stretching ratio of 3 times or more, TD stretching ratio of 5 times or more, MD stretching rate of 50-300% / s, and TD stretching rate of 50-300% / s.

[0139] According to the present invention, the method may or may not involve annealing and setting the stretched film. Preferably, the method includes annealing and setting the stretched film, wherein, when setting is performed, the annealing and setting temperature is preferably 160–180°C. The annealing and setting time is preferably 5–60 seconds. This annealing and setting treatment of the stretched film can improve the dimensional stability of the film.

[0140] According to the present invention, the method may further include subjecting the obtained polypropylene film to surface corona treatment, edge trimming, and winding, which are conventional operations in the art and are not particularly limited thereto.

[0141] The present invention will be further described below with reference to the embodiments, but the scope of the present invention is not limited to these embodiments.

[0142] In the following examples and comparative examples:

[0143] The film casting equipment was purchased from Labtech GmbH in Sweden, model LCR400.

[0144] The biaxial stretching equipment for thin films was purchased from Brückner GmbH, Germany, model Karo IV.

[0145] The properties of the modified polypropylene composition and the film were tested according to the following methods, and the film test results are shown in Tables 2 and 3.

[0146] 1. Determination of ash content in polypropylene / modified polypropylene grafted with alkenyl functional monomers:

[0147] The determination shall be carried out in accordance with the method specified in GB / T 9345-2008.

[0148] 2. Isotacticity determination of polypropylene:

[0149] The determination shall be carried out in accordance with the method specified in GB / T 2412-2008.

[0150] 3. Determination of Melt Flow Rate (MFR):

[0151] The MFR of polypropylene / grafted modified polypropylene was determined using a CEAST 7026 melt flow indexer at 230°C and a load of 2.16 kg, according to the method specified in GB / T 3682-2018.

[0152] 4. Melting temperature T m Measurement:

[0153] Differential scanning calorimetry (DSC) was used to analyze the melting and crystallization processes of polypropylene / grafted modified polypropylene. Specifically, under nitrogen protection, 5–10 mg of sample was heated from 20 °C to 200 °C using a three-stage heating and cooling method. Changes in heat flow were used to reflect the melting and crystallization processes, and the melting temperature T was calculated accordingly. m .

[0154] 5. Determination of parameter η:

[0155] Boil 1-2g of the grafted product under reflux in an appropriate amount of xylene until the particles are completely dissolved. While still hot, pour the xylene solution into 6 times its volume of organic solvent (ethyl acetate or acetone) to precipitate. Let the mixture stand for 1 hour until all insoluble matter precipitates out. Filter the mixture using a vacuum funnel. The filtered insoluble matter is the pure grafted product, which is then dried and weighed. The ratio of the grafted portion to the self-polymerized portion of the functional monomer structural unit is:

[0156]

[0157] In the formula, w0 is the mass of ungrafted polypropylene, w1 is the mass of the grafted product, and w2 is the mass of the insoluble matter.

[0158] 6. Determination of flexural modulus:

[0159] The determination shall be carried out in accordance with the method specified in GB / T 9341-2008.

[0160] 7. Determination of DC volume resistivity:

[0161] The determination shall be carried out in accordance with the method specified in GB / T 13542.2-2009.

[0162] 8. Determination of breakdown field strength:

[0163] The determination shall be carried out in accordance with the method specified in GB / T 13542.2-2009.

[0164] 9. Measurement of energy storage density and energy storage efficiency:

[0165] The determination should be performed according to the methods specified in the following literature.

[0166] Yuan,C.,Zhou,Y.,Zhu,Y.et al.Polymer / molecular semiconductor all-organic composites for high-temperature dielectric energy storage.NatCommun11,3919(2020).

[0167] 10. Determination of dielectric constant and dielectric loss factor:

[0168] The determination should be performed according to the methods specified in the following literature.

[0169] Yuan,C.,Zhou,Y.,Zhu,Y.et al.Polymer / molecular semiconductor all-organic composites for high-temperature dielectric energy storage.NatCommun11,3919(2020).

[0170] 11. Thickness of the capacitor film:

[0171] The determination shall be carried out in accordance with the method specified in GB / T 13542.3-2009.

[0172] 12. Characterization of the dispersed phase and calculation of D50:

[0173] Polypropylene / polypropylene modified material was hot-pressed and extruded to obtain strips, which were then immersed in liquid nitrogen for 15 minutes and fractured. The fracture surface was sputter-coated with gold, and the cross-section was characterized by scanning electron microscopy to obtain microscopic morphology images. Using analytical software, 200 dispersed phases from each sample were taken and their diameters measured. The D50 was calculated using data processing software. D50 represents the median particle size, which is the particle size corresponding to a cumulative particle size distribution percentage of 50% for a sample.

[0174] 13. Determination of tensile strength and elongation at break of thin films:

[0175] The determination shall be carried out in accordance with the method specified in GB / T 13542.2-2009.

[0176] 14. VOC determination:

[0177] VOCs were tested according to the VDA277 standard.

[0178] Example

[0179] The raw materials used in the examples are described in Tables A and B below.

[0180] Table A

[0181]

[0182]

[0183] *PP1: Polypropylene used in Examples 1, 4, 6, 10-14, and Comparative Examples 1, 3-5.

[0184] *PP2: Polypropylene used in Examples 2, 3, 5, 7, and 9.

[0185] *PP3: Polypropylene used in Example 8.

[0186] *PP4: Polypropylene used in Comparative Example 2.

[0187] Properties of the powders used in the examples (Table B)

[0188]

[0189] In all embodiments, the polypropylene powder used was sieved using a vibrating screen equipped with 16-mesh and 48-mesh sieves before the grafting reaction.

[0190] Example 1

[0191] (1) Preparation of modified polypropylene

[0192] 5.0 kg of PP1 powder, sieved through a sieve, was added to a 50 L reactor equipped with a double-layer four-bladed agitator and baffles. The reaction system was sealed, and nitrogen was used for purging to remove oxygen. A homogeneous solution of 7.2 g of tert-butyl peroxide (2-ethylhexanoate) and 400 g of styrene was added to the reactor and mixed with the powder for 30 minutes. Then, 17.8 kg of deoxygenated deionized water was added, and the mixture was heated to 50 °C for 2 hours to allow swelling. The swollen powder was then heated to 95 °C and reacted for 4 hours. After the reaction, the mixture was cooled, the liquid components were filtered off, and the product was vacuum dried at 70 °C for 10 hours to obtain polypropylene-g-styrene powder. Figure 1 The image shows the microstructure of the product from Example 1 under a 20,000x electron microscope. The brighter spherical portions are the dispersed phase composed of styrene structural units. It can be seen that the dispersed phase has a small particle size and a regular morphology.

[0193] (2) Preparation of modified polypropylene composition

[0194] Weigh the above-mentioned polypropylene-g-styrene powder, VOC inhibitor, antioxidant 1010 / 168 (weight ratio 1:1), and processing aids, and place them in a high-speed mixer. Mix at high speed for 30 seconds. Granulate using a Coperon WP25 twin-screw extruder. During processing, the twin-screw zone temperature is 190-200-210-220-230-230-210℃, and the screw speed is 300 rpm. Based on 100 parts by weight of modified polypropylene, the VOC inhibitor contains 0.5 parts by weight of fully vulcanized powdered silicone rubber, 0.25 parts by weight of zeolite powder, and 0.25 parts by weight of boehmite. The total amount of antioxidant is 0.3 parts by weight, and the amount of fluoropolymer processing aid is 0.1 parts by weight.

[0195] (3) Preparation of polypropylene capacitor film

[0196] The modified polypropylene composition granules obtained in step (2) were added to a hot air oven for drying, and the dried polypropylene composition granules were added to an LCR400 extrusion casting machine purchased from Labtech, Sweden for melt extrusion and casting. The temperature of the melt extrusion extruder was 230°C, the temperature of the screen changing zone was controlled at 230°C, the temperature of the die head was controlled at 230°C, and the temperature of the casting roller was controlled at 25°C to produce a thick cast sheet of modified polypropylene composition.

[0197] The modified polypropylene composition was cast into a thick sheet and placed in the stretching fixture of a biaxial stretching apparatus. A biaxial step-by-step stretching process was employed, involving longitudinal (MD) stretching followed by transverse (TD) stretching. The process conditions for each step are shown in Table 1: MD preheating temperature 155℃, MD stretching temperature 155℃, MD stretching ratio 5 times, MD stretching rate 200% / s; TD preheating temperature 170℃, TD stretching temperature 170℃, TD stretching ratio 7 times, film TD stretching rate 300% / s; film setting temperature 175℃. A biaxially oriented polypropylene capacitor film was obtained.

[0198] The obtained capacitor film was subjected to performance tests such as tensile properties and electrical properties. The performance parameters of the biaxially oriented polypropylene capacitor film are shown in Tables 2 and 3.

[0199] Example 2

[0200] (1) Preparation of modified polypropylene

[0201] 5.0 kg of PP2 powder, sieved through a sieve, was added to a 50 L reactor equipped with a double-layer four-bladed agitator and baffles. The reaction system was sealed, and nitrogen was used for purging to remove oxygen. A homogeneous solution of 13.5 g of tert-butyl peroxide (2-ethylhexanoate) and 1001 g of styrene was added to the reactor and stirred with the powder. The mixture was then heated to 40 °C for 3 hours to allow swelling. Next, 36.0 kg of deionized water, preheated to 40 °C and deoxygenated, was added through a feed tank. The reactor was then heated to 90 °C and reacted for 6 hours. After the reaction, the mixture was cooled, the liquid components were filtered off, and the product was vacuum-dried at 70 °C for 10 hours to obtain polypropylene-g-styrene powder. Figure 2 The image shows the microstructure of the product in Example 2 under a 20,000x electron microscope, where the spherical bright areas are the dispersed phase composed of styrene structural units.

[0202] (2) Preparation of modified polypropylene composition

[0203] The above-mentioned polypropylene-g-styrene powder, VOC inhibitor, antioxidant 1035, and processing aids were placed in a high-speed mixer and stirred at high speed for 30 seconds. Granulation was then performed using a Coperon WP25 twin-screw extruder. During processing, the twin-screw zone temperature was 190-200-210-220-230-230-210℃, and the screw speed was 300 rpm. Based on 100 parts by weight of modified polypropylene, the VOC inhibitor comprised 0.7 parts by weight of fully vulcanized powdered silicone rubber, 0.2 parts by weight of zeolite powder, and 0.1 parts by weight of boehmite; the antioxidant comprised 0.5 parts by weight; and the fluoropolymer processing aid comprised 0.2 parts by weight.

[0204] (3) Preparation of polypropylene capacitor film

[0205] In this embodiment, the film preparation method is the same as in Example 1, except that the biaxial stretching process conditions are different, as detailed in Table 1. The performance parameters of the obtained polypropylene capacitor film are shown in Tables 2 and 3.

[0206] Example 3

[0207] (1) Preparation of modified polypropylene

[0208] 5.0 kg of PP2 powder, sieved from the middle layer of a sieve, was added to a 50 L reactor equipped with a double-layer four-bladed agitator and baffles. The reaction system was sealed, and nitrogen was used for purging to remove oxygen. A homogeneous solution of 3.1 g benzoyl peroxide, 112 g styrene, and 13.9 g maleic anhydride was prepared and added to the reactor along with the powder. The mixture was stirred and allowed to swell at room temperature for 8 hours, then heated to 92 °C. 16.4 kg of deionized water, preheated to 92 °C and deoxygenated, was then added through a feed tank, and the reaction was continued for 4 hours. After the reaction, the mixture was cooled, the liquid components were filtered off, and the product was vacuum dried at 70 °C for 10 hours to obtain polypropylene-g-maleic anhydride / styrene powder. Figure 3 The image shows the microstructure of the powder in Example 3 under a 20,000x electron microscope. The spherical bright areas are the dispersed phase composed of maleic anhydride / styrene structural units.

[0209] (2) Preparation of modified polypropylene composition

[0210] The modified polypropylene, VOC inhibitor, antioxidant 1010 / 168 (weight ratio 1:1), and fluoropolymer were placed in a high-speed mixer and stirred at high speed for 30 seconds. Granulation was then performed using a Coperon WP25 twin-screw extruder. During processing, the twin-screw zone temperature was 190-200-210-220-230-230-210℃, and the screw speed was 300 rpm. Based on 100 parts by weight of modified polypropylene, the VOC inhibitor comprised 0.6 parts by weight of fully vulcanized powdered silicone rubber, 0.34 parts by weight of zeolite powder, and 0.06 parts by weight of boehmite; the total antioxidant content was 0.3 parts by weight; and the fluoropolymer content was 0.1 parts by weight.

[0211] (3) Preparation of polypropylene capacitor film

[0212] In this embodiment, the film preparation method is the same as in Example 1, except that the biaxial stretching process conditions are different, as detailed in Table 1. The performance parameters of the obtained polypropylene capacitor film are shown in Tables 2 and 3.

[0213] Example 4

[0214] (1) Preparation of modified polypropylene

[0215] 5.0 kg of PP1 powder, sieved through a sieve, was added to a 50 L reactor equipped with a double-layer four-bladed agitator and baffles. The reaction system was sealed, and nitrogen was used for purging to remove oxygen. A homogeneous solution of 2.5 g benzoyl peroxide and 250.5 g methyl methacrylate was added to the reactor and mixed with the powder for 30 min. Then, 26.3 kg of deoxygenated deionized water was added. The reactor was heated to 91 °C and reacted for 3 hours. After the reaction, the mixture was cooled, the liquid components were filtered off, and the product was vacuum dried at 70 °C for 10 hours to obtain polypropylene-g-methyl methacrylate powder.

[0216] (2) Preparation of modified polypropylene composition

[0217] The above-mentioned polypropylene-g-methyl methacrylate, VOC inhibitor, antioxidant 1024, and fluoropolymer were placed in a high-speed mixer and stirred at high speed for 30 seconds. Granulation was then performed using a Coperon WP25 twin-screw extruder. During processing, the twin-screw zone temperature was 190-200-210-220-230-230-210℃, and the screw speed was 300 rpm. Based on 100 parts by weight of modified polypropylene, the VOC inhibitor comprised 0.5 parts by weight of fully vulcanized powdered silicone rubber, 0.4 parts by weight of zeolite powder, and 0.1 parts by weight of boehmite; the antioxidant comprised 0.3 parts by weight; and the fluoropolymer comprised 0.1 parts by weight.

[0218] (3) Preparation of polypropylene capacitor film

[0219] In this embodiment, the film preparation method is the same as in Example 1, except that the biaxial stretching process conditions are different, as detailed in Table 1. The performance parameters of the obtained polypropylene capacitor film are shown in Tables 2 and 3.

[0220] Example 5

[0221] (1) Preparation of modified polypropylene

[0222] 5.0 kg of PP2 powder, sieved from the middle layer of a sieve, was added to a 50 L reactor equipped with a double-layer four-bladed agitator and baffles. The reaction system was sealed, and nitrogen was used for purging to remove oxygen. A homogeneous solution of 6.2 g benzoyl peroxide, 198.0 g styrene, and 52.0 g maleic anhydride was prepared and added to the reactor along with the powder. The mixture was stirred and allowed to swell at room temperature for 6 hours, then heated to 90 °C. 22.6 kg of deionized water, preheated to 90 °C and deoxygenated, was then added through a feed tank, and the reaction was continued for 4 hours. After the reaction, the mixture was cooled, the liquid components were filtered off, and the product was vacuum dried at 70 °C for 10 hours to obtain polypropylene-g-maleic anhydride / styrene powder.

[0223] (2) Preparation of modified polypropylene composition

[0224] The above-mentioned polypropylene-g-styrene / maleic anhydride, VOC inhibitor, antioxidant 1010 / 168 (weight ratio 1:1) and fluoropolymer were placed in a high-speed mixer and stirred at high speed for 30 seconds. Granulation was then performed using a Coperon WP25 twin-screw extruder. During processing, the twin-screw zone temperature was 190-200-210-220-230-230-210℃, and the screw speed was 300 rpm. Based on 100 parts by weight of modified polypropylene, the VOC inhibitor contained 1.0 parts by weight of fully vulcanized powdered silicone rubber, 0.6 parts by weight of zeolite powder, and 0.4 parts by weight of boehmite; the total amount of antioxidant was 0.3 parts by weight; and the amount of fluoropolymer was 0.1 parts by weight.

[0225] (3) Preparation of polypropylene capacitor film

[0226] In this embodiment, the film preparation method is the same as in Example 1, except that the biaxial stretching process conditions are different, as detailed in Table 1. The performance parameters of the obtained polypropylene capacitor film are shown in Tables 2 and 3.

[0227] Example 6

[0228] (1) Preparation of modified polypropylene

[0229] 5.0 kg of PP1 powder, sieved through a sieve, was added to a 50 L reactor equipped with a double-layer four-bladed agitator and baffles. The reaction system was sealed, and nitrogen was used for purging to remove oxygen. A homogeneous solution of 31 g lauroyl peroxide and 603 g vinyltriethoxysilane was prepared and added to the reactor, where it was stirred and mixed with the powder for 20 min. Then, 19.6 kg of deoxygenated deionized water was added. The reactor was heated to 91 °C and reacted for 7 hours. After the reaction, the mixture was cooled, the liquid components were filtered off, and the product was vacuum dried at 70 °C for 10 hours to obtain polypropylene-g-vinyltriethoxysilane powder.

[0230] (2) The powder obtained above was used to prepare a modified polypropylene composition, which was then granulated and used to prepare a film product. The method and conditions were the same as in Example 1. The performance parameters of the obtained polypropylene capacitor film are shown in Tables 2 and 3.

[0231] Example 7

[0232] (1) Preparation of modified polypropylene

[0233] 5.0 kg of PP2 powder, sieved from the middle layer of a sieve, was added to a 50 L reactor equipped with a double-layer four-bladed agitator and baffles. The reaction system was sealed, and nitrogen was used for purging to remove oxygen. A homogeneous solution of 6.2 g benzoyl peroxide, 115.0 g methyl acrylate, and 38.0 g acrylic acid was prepared and added to the reactor, where it was stirred and mixed with the powder for 40 min. The temperature was then raised to 95 °C. 36.1 kg of deionized water, preheated to 90 °C and deoxygenated, was then added through a feeding tank, and the reaction was continued for 4 hours. After the reaction, the mixture was cooled, the liquid components were filtered off, and the product was vacuum dried at 70 °C for 10 hours to obtain polypropylene-g-methyl acrylate / acrylic acid powder.

[0234] (2) The powder obtained above was used to prepare a modified polypropylene composition, which was then granulated and used to prepare a film product. The method and conditions were the same as in Example 1. The performance parameters of the obtained polypropylene capacitor film are shown in Tables 2 and 3.

[0235] Example 8

[0236] The PP1 powder in Example 1 was replaced with PP3 powder sieved using a sieve. All other preparation conditions and methods were the same as in Example 1. The performance parameters of the resulting polypropylene film were tested. The results are shown in Tables 2 and 3.

[0237] Example 9

[0238] (1) Preparation of modified polypropylene

[0239] 5.0 kg of PP2 powder, sieved through a sieve, was added to a 50 L reactor equipped with a double-layer four-bladed agitator and baffles. The reaction system was sealed, and nitrogen was used for purging to remove oxygen. A homogeneous solution of 8.8 g of benzoyl peroxide and 355 g of 4-vinylpyridine was added to the reactor and stirred for 30 minutes. Then, 27.8 kg of deoxygenated deionized water was added, and the mixture was heated to 50 °C for 2 hours to allow swelling. The reactor was then heated to 92 °C and reacted for 6 hours. After the reaction, the mixture was cooled, the liquid components were filtered off, and the product was vacuum-dried at 70 °C for 10 hours to obtain polypropylene-g-4-vinylpyridine powder.

[0240] (2) The powder obtained above was used to prepare a modified polypropylene composition, which was then granulated and used to prepare a film product. The method and conditions were the same as in Example 1. The performance parameters of the obtained polypropylene capacitor film are shown in Tables 2 and 3.

[0241] Example 10

[0242] (1) Preparation of modified polypropylene

[0243] 5.0 kg of PP1 powder, sieved through a sieve, was added to a 50 L reactor equipped with a double-layer four-bladed agitator and baffles. The reaction system was sealed, and nitrogen was used for purging to remove oxygen. A homogeneous solution of 1.35 g benzoyl peroxide and 76 g glycidyl methacrylate was added to the reactor and mixed with the powder for 30 min. Then, 16.7 kg of deoxygenated deionized water was added. The reactor was heated to 93 °C and reacted for 2.5 hours. After the reaction, the mixture was cooled, the liquid components were filtered off, and the product was vacuum dried at 70 °C for 10 hours to obtain polypropylene-glycidyl methacrylate powder. Figure 4 This is a microscopic image of the powder in Example 10 under a 20,000x electron microscope, where the spherical phase with higher brightness is the dispersed phase.

[0244] (2) The powder obtained above was used to prepare a modified polypropylene composition, which was then granulated and used to prepare a film product. The method and conditions were the same as in Example 1. The performance parameters of the obtained polypropylene capacitor film are shown in Tables 2 and 3.

[0245] Example 11

[0246] The modified polypropylene composition and polypropylene capacitor film were prepared according to the method of Example 1, except that the VOC inhibitor was 0.1 parts by weight of fully vulcanized powdered silicone rubber, 0.06 parts by weight of zeolite powder, and 0.04 parts by weight of pseudoboehmite. The performance parameters of the obtained polypropylene capacitor film are shown in Tables 2 and 3.

[0247] Example 12

[0248] The modified polypropylene composition and polypropylene capacitor film were prepared according to the method of Example 2, except that the VOC inhibitor was 0.2 parts by weight of fully vulcanized powdered silicone rubber, 0.1 parts by weight of zeolite powder, and 0.1 parts by weight of pseudoboehmite. The performance parameters of the obtained polypropylene capacitor film are shown in Tables 2 and 3.

[0249] Example 13

[0250] The PP1 powder screened out from the middle layer of the screening machine in Example 1 was replaced with the PP1 powder screened out from the upper layer of the screening machine. Other preparation conditions and methods were the same as in Example 1. The performance parameters of the resulting polypropylene capacitor film are shown in Tables 2 and 3.

[0251] Example 14

[0252] The PP1 powder screened out from the middle layer of the screening machine in Example 1 was replaced with the PP1 powder screened out from the bottom layer of the screening machine. Other preparation conditions and methods were the same as in Example 1. The performance parameters of the resulting polypropylene capacitor film are shown in Tables 2 and 3.

[0253] Comparative Example 1

[0254] 5.0 kg of PP1 powder sieved from the middle layer of a sieving machine was used for granulation and film preparation. Other preparation conditions and methods were the same as in Example 1. The performance parameters of the obtained products were tested. The results are shown in Tables 2 and 3. Figure 5 This is a microscopic image of PP1 powder under a 20,000x electron microscope, showing no visible dispersed phase.

[0255] Comparative Example 2

[0256] The PP1 powder in Example 1 was replaced with PP4 powder sieved through a sieve. The amount of deionized water added was 10.8 kg. The VOC inhibitor consisted of 0.1 parts by weight of fully vulcanized powdered silicone rubber, 0.06 parts by weight of zeolite powder, and 0.04 parts by weight of boehmite. Other preparation conditions and methods were the same as in Example 1. The performance parameters of the obtained product were tested. The results are shown in Tables 2 and 3.

[0257] Comparative Example 3

[0258] 5.0 kg of PP1 powder, sieved through a sieve, was added to a 50 L reactor equipped with a double-layer four-bladed agitator and baffles. The reaction system was sealed, and nitrogen was used for purging to remove oxygen. A homogeneous solution of 7.5 g of benzoyl peroxide and 500 g of n-butyl methacrylate was prepared and added to the reactor, where it was stirred and mixed with the powder for 30 min. Then, 16.5 kg of deoxygenated deionized water was added. The reactor was heated to 93 °C and reacted for 2.5 hours. After the reaction, the mixture was cooled, the liquid components were filtered off, and the product was vacuum dried at 70 °C for 10 hours to obtain polypropylene-g-n-butyl methacrylate powder.

[0259] The powder obtained above was used to prepare a modified polypropylene composition, which was then granulated and used to prepare film products, using the same methods and conditions as in Example 1. The performance parameters of the obtained polypropylene capacitor film are shown in Tables 2 and 3.

[0260] Comparative Example 4

[0261] 5.0 kg of PP1 powder sieved from the middle layer of a sieve was mixed with 400 g of polystyrene GPPS-123 for granulation and film preparation. The VOC inhibitor consisted of 0.2 parts by weight of fully vulcanized powdered silicone rubber, 0.2 parts by weight of zeolite powder, and 0.1 parts by weight of boehmite. Other preparation conditions and methods were the same as in Example 1. The performance parameters of the obtained product were tested. The results are shown in Tables 2 and 3.

[0262] Comparative Example 5

[0263] 5.0 kg of PP1 powder sieved from the middle layer of a sieve was added to 1000 g of polystyrene GPPS-123 for granulation and film product preparation. Other preparation conditions and methods were the same as in Example 2. During biaxial stretching film preparation, the film ruptured.

[0264] Comparative Example 6

[0265] The performance parameters of the copper peak MPP03 high-temperature membrane were tested, and the results are shown in Tables 2 and 3.

[0266]

[0267]

[0268]

[0269] A comparison of D1 and C1 shows that grafting modification can significantly improve the dielectric and energy storage properties of polypropylene.

[0270] A comparison of D2 and C1 shows that when high-ash polypropylene is used as the reaction raw material, even under the same preparation conditions, the grafted phase is smaller, and its energy storage efficiency and energy storage performance are significantly lower than those of low-ash polypropylene modifiers.

[0271] By comparing D3 and C1-C14, it can be seen that if the dispersed phase size is too large, the breakdown strength of the product is almost not improved compared to D1, and other dielectric properties and energy storage properties are not significantly improved compared to D1, which is significantly different from the grafted modification examples.

[0272] A comparison of D4 and C1-C14 shows that by directly adding grafted monomer polymers, the interfacial forces between the grafted monomer polymers and polypropylene are weaker, the breakdown strength is lower, and the energy storage performance is actually lower than that of D1.

[0273] A comparison of D5 and C2 shows that even with a high amount of functional monomers added, the polypropylene graft-modified material can still form a film normally. However, after adding a large amount of functional monomer polymers, the material cracks during processing and cannot form a film.

[0274] By comparing D6 and C1-C14, it can be seen that the energy storage efficiency of the capacitor film of the present invention at 120°C is significantly higher than that of commercially available high-temperature capacitor films, and the energy storage density and dielectric properties are also comparable to or slightly better than those of commercially available high-temperature capacitor films.

[0275] By comparing C1, C11-C12 and D1-D5, it can be seen that the use of VOC inhibitors can significantly reduce the VOC content of the modified polypropylene composition, and the use of a VOC inhibitor composed of three components can further improve the electrical insulation performance of the film.

[0276] As can be seen from C13-C14, controlling the particle size of the polypropylene base material to the optimal range can give the product better insulation and energy storage properties.

[0277] The various embodiments of the present invention have been described above. These descriptions are exemplary and not exhaustive, nor are they limited to the disclosed embodiments. Many modifications and variations will be apparent to those skilled in the art without departing from the scope and spirit of the described embodiments.

[0278] The endpoints and any values ​​of the ranges disclosed herein are not limited to the precise ranges or values, and these ranges or values ​​should be understood to include values ​​close to these ranges or values. For numerical ranges, the endpoint values ​​of the various ranges, the endpoint values ​​of the various ranges and individual point values, and individual point values ​​can be combined with each other to obtain one or more new numerical ranges, which should be considered as specifically disclosed herein.

Claims

1. A low-VOC modified polypropylene composition, the modified polypropylene composition comprising modified polypropylene grafted with alkenyl functional monomers, a VOC inhibitor, an antioxidant, and a processing aid; The modified polypropylene grafted with alkenyl functional monomers comprises structural units derived from polypropylene as the matrix phase and structural units derived from alkenyl functional monomers as the dispersed phase; the ash content of the modified polypropylene grafted with alkenyl functional monomers is less than 50 ppm; the mass ratio of structural units derived from alkenyl functional monomers and in the grafted state to structural units derived from alkenyl functional monomers and in the self-polymerized state in the modified polypropylene grafted with alkenyl functional monomers is greater than or equal to 1.0; and the D50 of the dispersed phase is less than 450 nm. The polypropylene has a particle size of 16-50 mesh, an ash content of less than 55 ppm, and a flexural modulus of 1400-2000 MPa.

2. The low-VOC modified polypropylene composition according to claim 1, wherein, The ash content of the modified polypropylene grafted with the alkenyl functional monomer is less than 36 ppm.

3. The low-VOC modified polypropylene composition according to claim 2, wherein, The ash content of the modified polypropylene grafted with the alkenyl functional monomer is less than 30 ppm.

4. The low-VOC modified polypropylene composition according to claim 1, wherein, In the modified polypropylene grafted with alkenyl functional monomers, the mass ratio of structural units derived from alkenyl functional monomers and in the grafted state to structural units derived from alkenyl functional monomers and in the self-polymerized state is 1.1 to 10.

5. The low-VOC modified polypropylene composition according to claim 4, wherein, In the modified polypropylene grafted with alkenyl functional monomers, the mass ratio of structural units derived from alkenyl functional monomers and in the grafted state to structural units derived from alkenyl functional monomers and in the self-polymerized state is 1.2 to 6.

6. The low-VOC modified polypropylene composition according to claim 1, wherein, The D50 of the dispersed phase is 50~400 nm.

7. The low-VOC modified polypropylene composition according to claim 1, wherein, The modified polypropylene grafted with the alkenyl functional monomer has at least one of the following characteristics: a melt flow rate of 1~10 g / 10min at 230 °C and 2.16 kg load; and a melting temperature T. m Temperature range: 155~168 ℃; flexural modulus range: 1400~2000 MPa.

8. The low-VOC modified polypropylene composition according to claim 7, wherein, The melt flow rate at 230 °C and 2.16 kg load is 1.5~8 g / 10min.

9. The low-VOC modified polypropylene composition according to claim 8, wherein, The melt flow rate at 230 °C and 2.16 kg load is 2~5 g / 10min.

10. The low-VOC modified polypropylene composition according to claim 7, wherein, Melting temperature T m The temperature ranges from 157 to 165 degrees Celsius.

11. The low-VOC modified polypropylene composition according to claim 7, wherein, The flexural modulus is 1500~1800 MPa.

12. The low-VOC modified polypropylene composition according to claim 1, wherein, The modified polypropylene grafted with alkenyl functional monomers has at least one of the following characteristics: - Maximum operating temperature ≥100 ℃; Breakdown field strength E at -120 ℃ g ≥510 MV / m; DC volume resistivity ρ at -120 ℃ and 200 MV / m electric field strength vg ≥6.0×10 13 Ω m; The dielectric constant at -120 ℃ and 100 Hz is greater than 2.25; The dielectric loss at -120 ℃ and 100 Hz is less than 1.5E-3; The energy storage density at -120 ℃ and 300 MV / m is greater than 0.720 J / cm³. 3 ; The energy storage efficiency at -120 ℃ and 300 MV / m is greater than 90.0%.

13. The low-VOC modified polypropylene composition according to claim 12, wherein, The modified polypropylene grafted with alkenyl functional monomers has at least one of the following characteristics: - Maximum operating temperature is 110~160 ℃; Breakdown field strength E at -120 ℃ g The value is 550~800 MV / m; DC volume resistivity ρ at -120 ℃ and 200 MV / m electric field strength vg 1.0×10 14 Ω m~1.0×10 20 Ω m; The dielectric constant at -120 ℃ and 100 Hz is 2.26~2.65; The dielectric loss at -120 ℃ and 100 Hz is 1.0E-6~1.3E-3; The energy storage density at -120 ℃ and 300 MV / m is 0.740~2.0 J / cm³. 3 ; The energy storage efficiency at -120 ℃ and 300 MV / m is 92.0 ~ 99.0%.

14. The low-VOC modified polypropylene composition according to claim 13, wherein, The maximum operating temperature is 120~145℃.

15. The low-VOC modified polypropylene composition according to claim 1, wherein, The alkenyl-containing functional monomer is selected from at least one monomer having the structure shown in Formula 1. Formula 1 In Equation 1, R b R c R d Each is independently selected from H, substituted or unsubstituted alkyl groups; R a Selected from substituted or unsubstituted alkyl groups, substituted or unsubstituted alkoxy groups, substituted or unsubstituted aryl groups, substituted or unsubstituted ester groups, substituted or unsubstituted carboxyl groups, substituted or unsubstituted cycloalkyl or heterocyclic groups, cyano groups, and substituted or unsubstituted silyl groups; R a and R d Arrange the rings arbitrarily.

16. The low-VOC modified polypropylene composition according to claim 15, wherein, R b R c R d Each is independently selected from H, substituted or unsubstituted C1-C6 alkyl groups; R a Selected from substituted or unsubstituted C1-C 20 Alkyl, substituted or unsubstituted C1-C 20 Alkoxy, substituted or unsubstituted C6-C 20 aryl, substituted or unsubstituted C1-C 20 Ester group, substituted or unsubstituted C1-C 20 Carboxyl, substituted or unsubstituted C3-C 20 Cycloalkyl or heterocyclic, cyano, substituted or unsubstituted C3-C 20 Silyl group; the substituted group is halogen, -OH, -NH2, =O, C1-C 12 Alkyl, C3-C6 cycloalkyl, C1-C 12 alkoxy groups, C1-C 12 Acyloxy group; R a and R d Optionally, it can form a 4-6 membered heterocycle with a double bond.

17. The low-VOC modified polypropylene composition according to claim 16, wherein, R b R c R d Each is independently selected from H, substituted or unsubstituted C1-C6 alkyl groups; R a It is selected from at least one of the groups shown in Formula 2, Formula 3, Formula 4, Formula 5, Formula 6, and heterocyclic groups; Formula 2 In Equation 2, R 4 -R 8 Each is independently selected from H, halogen, hydroxyl, amino, phosphate group, sulfonic acid group, substituted or unsubstituted C1-C. 12 Alkyl, substituted or unsubstituted C3-C 12 cycloalkyl, substituted or unsubstituted C1-C 12 alkoxy, substituted or unsubstituted C1-C 12 ester group, substituted or unsubstituted C1-C 12 The substituted amino group, wherein the substituted group is selected from halogen, hydroxyl, amino, phosphate, sulfonic acid, C1-C 12 Alkyl, C3-C 12 cycloalkyl, C1-C 12 alkoxy groups, C1-C 12 ester group, C1-C 12 The amino group; Formula 3 In Equation 3, R4-R 10 Each is independently selected from H, halogen, hydroxyl, amino, phosphate group, sulfonic acid group, substituted or unsubstituted C1-C. 12 Alkyl, substituted or unsubstituted C3-C 12 cycloalkyl, substituted or unsubstituted C1-C 12 alkoxy, substituted or unsubstituted C1-C 12 ester group, substituted or unsubstituted C1-C 12 The substituted amino group, wherein the substituted group is selected from halogen, hydroxyl, amino, phosphate, sulfonic acid, C1-C 12 Alkyl, C3-C 12 cycloalkyl, C1-C 12 alkoxy groups, C1-C 12 ester group, C1-C 12 The amino group; Formula 4 In Equation 4, R4'-R 10 Each group is independently selected from H, halogen, hydroxyl, amino, phosphate, sulfonic acid, substituted or unsubstituted C1-C. 12 Alkyl, substituted or unsubstituted C3-C 12 cycloalkyl, substituted or unsubstituted C1-C 12 alkoxy, substituted or unsubstituted C1-C 12 ester group, substituted or unsubstituted C1-C 12 The substituted amino group, wherein the substituted group is selected from halogen, hydroxyl, amino, phosphate, sulfonic acid, C1-C 12 Alkyl, C3-C 12 cycloalkyl, C1-C 12 alkoxy groups, C1-C 12 ester group, C1-C 12 The amino group; Formula 5 In Equation 5, R', R'', and R''' are each independently selected from substituted or unsubstituted C1-C. 12 Straight-chain alkyl, substituted or unsubstituted C3-C 12 Branched alkyl, substituted or unsubstituted C1-C 12 alkoxy, substituted or unsubstituted C1-C 12 Acyloxy group; Formula 6 In Equation 6, R m Selected from hydroxyl groups and / or substituted or unsubstituted groups: C1-C 20 Straight-chain alkyl, C3-C 20 Branched alkyl, C3-C 12 cycloalkyl, C3-C 12 Epoxyalkyl, C3-C 12 Epoxyalkylalkyl, wherein the substituted group is selected from at least one of halogen, amino and hydroxyl groups; The heterocyclic group is selected from imidazole, pyrazol, carbazole, pyrrolidone, pyridinyl, piperidinyl, caprolactam, pyrazinyl, thiazolyl, purine, morpholino, and oxazolino.

18. The low-VOC modified polypropylene composition according to claim 17, wherein, R 4 -R 8 Each is independently selected from H, halogen, hydroxyl, amino, substituted or unsubstituted C1-C6 alkyl, substituted or unsubstituted C1-C6 alkoxy.

19. The low-VOC modified polypropylene composition according to claim 17, wherein, R4-R 10 Each of the groups is independently selected from H, halogen, hydroxyl, amino, substituted or unsubstituted C1-C6 alkyl, substituted or unsubstituted C1-C6 alkoxy, wherein the substituted group is selected from halogen, hydroxyl, amino, C1-C6 alkyl, C1-C6 alkoxy.

20. The low-VOC modified polypropylene composition according to claim 17, wherein, R4'-R 10 Each of the groups is independently selected from H, halogen, hydroxyl, amino, substituted or unsubstituted C1-C6 alkyl, substituted or unsubstituted C1-C6 alkoxy, wherein the substituted group is selected from halogen, hydroxyl, amino, C1-C6 alkyl, C1-C6 alkoxy.

21. The low-VOC modified polypropylene composition according to claim 17, wherein, R', R'', and R''' are each independently selected from substituted or unsubstituted C1-C6 straight-chain alkyl, substituted or unsubstituted C3-C6 branched alkyl, substituted or unsubstituted C1-C6 alkoxy, or substituted or unsubstituted C1-C6 acyloxy.

22. The low-VOC modified polypropylene composition according to claim 17, wherein, The alkenyl-containing functional monomer is a styrene monomer, which is selected from at least one of styrene, α-methylstyrene, 1-vinylnaphthalene, 2-vinylnaphthalene, monosubstituted or polysubstituted styrene, monosubstituted or polysubstituted α-methylstyrene, monosubstituted or polysubstituted 1-vinylnaphthalene, and monosubstituted or polysubstituted 2-vinylnaphthalene.

23. The low-VOC modified polypropylene composition according to claim 22, wherein, The substituted group is selected from at least one of halogen, hydroxyl, amino, phosphate, sulfonic acid, C1-C8 straight-chain alkyl, C3-C8 branched alkyl or cycloalkyl, C1-C6 straight-chain alkoxy, C3-C8 branched alkoxy or cycloalkoxy, C1-C8 straight-chain ester, C3-C8 branched ester or cycloester, C1-C8 straight-chain amino, and C3-C8 branched amino or cycloamino.

24. The low-VOC modified polypropylene composition according to claim 23, wherein, The styrene monomer is selected from at least one of styrene, α-methylstyrene, 2-methylstyrene, 3-methylstyrene, and 4-methylstyrene.

25. The low-VOC modified polypropylene composition according to claim 17, wherein, The alkenyl-containing functional monomer is an alkenyl-containing silane monomer, which is selected from at least one of vinyltriethoxysilane, vinyltrimethoxysilane, vinyltriisopropoxysilane, vinyltritert-butoxysilane, vinyltriacetoxysilane, methylvinyldimethoxysilane, ethylvinyldiethoxysilane, allyltriethoxysilane, allyltrimethoxysilane, allyltriisopropoxysilane, vinyltri(β-methoxyethoxy)silane, allyltri(β-methoxyethoxy)silane, allyltritert-butoxysilane, allyltriacetoxysilane, methylallyldimethoxysilane, and ethylallyldiethoxysilane.

26. The low-VOC modified polypropylene composition according to claim 17, wherein, The alkenyl-containing functional monomer is an acrylate monomer and / or an acrylic monomer.

27. The low-VOC modified polypropylene composition according to claim 26, wherein, The acrylate monomers are selected from at least one of methyl methacrylate, sec-butyl methacrylate, ethyl methacrylate, n-butyl methacrylate, isobutyl methacrylate, tert-butyl methacrylate, isooctyl methacrylate, dodecyl methacrylate, coconut oleate methacrylate, octadecyl methacrylate, dimethylaminoethyl methacrylate, diethylaminoethyl methacrylate, dimethylaminopropyl methacrylate, and glycidyl methacrylate.

28. The low-VOC modified polypropylene composition according to claim 26, wherein, The acrylic monomer is selected from at least one of acrylic acid, methacrylic acid and 2-ethylacrylic acid.

29. The low-VOC modified polypropylene composition according to claim 16, wherein, The alkenyl-containing functional monomer is at least one of maleic anhydride, maleimide and its derivatives, itaconic anhydride, and α-methylene-γ-butyrolactone.

30. The low-VOC modified polypropylene composition according to claim 29, wherein, The alkenyl-containing functional monomer is maleic anhydride.

31. The low-VOC modified polypropylene composition according to claim 1, wherein, The ash content of the polypropylene is less than 40 ppm.

32. The low-VOC modified polypropylene composition according to claim 31, wherein, The ash content of the polypropylene is less than 35 ppm.

33. The low-VOC modified polypropylene composition according to claim 1, wherein, The flexural modulus of the polypropylene is 1500~1800 MPa.

34. The low-VOC modified polypropylene composition according to claim 1, wherein, The polypropylene is either homopolymer polypropylene or copolymer polypropylene.

35. The low-VOC modified polypropylene composition according to claim 34, wherein, The polypropylene has at least one of the following characteristics: The melt flow rate at -230 ℃ and 2.16 kg load is 0.5~10 g / 10 min; -Melting temperature T m Temperatures above 150°C; -Isotacticity greater than 96%; or, the total content of ethylene and butene units is less than 3.0 mol%, or greater than 0.1 mol% and less than or equal to 3.0 mol%.

36. The low-VOC modified polypropylene composition according to claim 35, wherein, The polypropylene has at least one of the following characteristics: The melt flow rate at -230 ℃ and 2.16 kg load is 1~5 g / 10 min; -Melting temperature T m The temperature ranges from 153 to 180 degrees Celsius. -Isotacticity greater than 96.5%; or, the total content of ethylene and butene units is greater than 0 and less than 0.1 mol.

37. The low-VOC modified polypropylene composition according to claim 36, wherein, The polypropylene has at least one of the following characteristics: The melt flow rate at -230 ℃ and 2.16 kg load is 2~4 g / 10 min; -Melting temperature T m The temperature ranges from 155 to 167 degrees Celsius.

38. The low-VOC modified polypropylene composition according to claim 1, wherein, The modified polypropylene grafted with the alkenyl functional monomer is prepared by a method comprising the following steps: in the presence of an inert gas, a reaction mixture comprising polypropylene powder and an alkenyl functional monomer is subjected to a grafting reaction to obtain the modified polypropylene grafted with the alkenyl functional monomer.

39. The low-VOC modified polypropylene composition according to claim 38, wherein, The reaction mixture also includes a free radical initiator.

40. The low-VOC modified polypropylene composition according to claim 39, wherein, The free radical initiator is selected from peroxide free radical initiators and / or azo free radical initiators.

41. The low-VOC modified polypropylene composition according to claim 40, wherein, The peroxide radical initiator is selected from at least one of benzoyl peroxide, dicumyl peroxide, di-tert-butyl peroxide, lauroyl peroxide, dodecyl peroxide, tert-butyl peroxide, diisopropyl peroxide, tert-butyl peroxide, and dicyclohexyl peroxide; the azo radical initiator is azobisisobutyronitrile and / or azobisisoheptanenitrile.

42. The low-VOC modified polypropylene composition according to claim 39, wherein, The mass ratio of the free radical initiator to the alkenyl-containing functional monomer is 0.1~10:

100.

43. The low-VOC modified polypropylene composition according to claim 42, wherein, The mass ratio of the free radical initiator to the alkenyl-containing functional monomer is 0.5~5:

100.

44. The low-VOC modified polypropylene composition according to claim 39, wherein, The reaction mixture further includes at least one of the following components: deionized water and / or an organic solvent, wherein the mass content of the deionized water is 300-800% of the total mass of the polypropylene powder and the alkenyl functional monomer, and the mass content of the organic solvent is 1-35% of the mass of the polypropylene powder.

45. The low-VOC modified polypropylene composition according to claim 44, wherein, The preparation method of the modified polypropylene grafted with the alkenyl functional monomer includes the following steps: a. Place the polypropylene powder in a closed reactor and replace it with an inert gas; b. Add the free radical initiator and the alkenyl-containing functional monomer to the closed reactor and stir to mix; c. Add deionized water and heat the reaction system to the grafting reaction temperature to carry out the grafting reaction; optionally, allow the reaction system to swell before or after adding deionized water; d. After the reaction is complete, the mixture is filtered and dried to obtain the modified polypropylene grafted with the alkenyl functional monomer.

46. ​​The low-VOC modified polypropylene composition according to claim 44, wherein, The preparation method of the modified polypropylene grafted with the alkenyl functional monomer includes the following steps: a. Place the polypropylene powder in a closed reactor and replace it with an inert gas; b. Mix the organic solvent and the free radical initiator, and add them to the closed reactor; c. Remove the organic solvent, add an alkenyl-containing functional monomer, and optionally swell the reaction system; d. Add deionized water to raise the temperature of the reaction system to the grafting reaction temperature and carry out the grafting reaction; e. After the reaction is complete, the mixture is filtered and dried to obtain the modified polypropylene grafted with the alkenyl functional monomer.

47. The low-VOC modified polypropylene composition according to any one of claims 38-46, wherein, It also includes a screening and pretreatment step for polypropylene powder.

48. The low-VOC modified polypropylene composition according to claim 47, wherein, The screening pretreatment includes the following steps: screening the powder using a double-layer vibrating screen or linear screen equipped with a screen of appropriate mesh size, and using the polypropylene powder in the middle layer of the screening machine as the reaction material.

49. The low-VOC modified polypropylene composition according to any one of claims 38-46, wherein, The grafting reaction is carried out at a temperature of 30~110 ℃ for 0.5~10 h.

50. The low-VOC modified polypropylene composition according to claim 49, wherein, The grafting reaction is carried out at a temperature of 60-95 °C for 1-6 h.

51. The low-VOC modified polypropylene composition according to claim 1, wherein, Based on 100 parts by weight of modified polypropylene, the content of the VOC inhibitor is 0.1 to 3 parts by weight; the content of the antioxidant is 0.1 to 0.8 parts by weight; and the content of the processing aid is 0.05 to 1 part by weight.

52. The low-VOC modified polypropylene composition according to claim 51, wherein, Based on 100 parts by weight of modified polypropylene, the content of the VOC inhibitor is 0.5 to 2 parts by weight; the content of the antioxidant is 0.1 to 0.5 parts by weight; and the content of the processing aid is 0.05 to 0.5 parts by weight.

53. The low-VOC modified polypropylene composition according to any one of claims 1-46, wherein, The VOC inhibitor comprises the following components: fully vulcanized powdered silicone rubber, zeolite powder, and boehmite; wherein, based on the total weight of the VOC inhibitor, the content of fully vulcanized powdered silicone rubber is 8wt%~70wt%; the content of zeolite powder is 10wt%~65wt%; and the content of boehmite is 5wt%~40wt%.

54. The low-VOC modified polypropylene composition according to claim 1, wherein, Based on the total weight of VOC inhibitors, the content of fully vulcanized powdered silicone rubber is 50wt%~70wt%; the content of zeolite powder is 15wt%~40wt%; and the content of boehmite is 6wt%~25wt%.

55. The low-VOC modified polypropylene composition according to claim 54, wherein, The average particle size of the fully vulcanized powdered silicone rubber is 0.05~1μm; the rubber particles have a cross-linked structure and a gel content of more than 60wt%. The specific surface area of ​​the zeolite powder is 100~400 m². 2 / gr; average pore size is 0.1~20nm; fineness is 1000~2500 mesh; The specific surface area of ​​the pseudoboehmite is 100~350m². 2 / gr; average pore size is 2~60nm.

56. The low-VOC modified polypropylene composition according to claim 55, wherein, The average particle size of the rubber particles in the fully vulcanized powdered silicone rubber is 0.05~0.2μm; the rubber particles have a cross-linked structure and a gel content of more than 75wt%.

57. The low-VOC modified polypropylene composition according to claim 56, wherein, The average particle size of the fully vulcanized powdered silicone rubber is 0.05~0.1μm; the rubber particles have a cross-linked structure and a gel content of more than 90wt%.

58. The low-VOC modified polypropylene composition according to claim 55, wherein, The specific surface area of ​​the zeolite powder is 150~300 m². 2 / gr; average pore size is 0.3~15nm; fineness is 1200~2500 mesh.

59. The low-VOC modified polypropylene composition according to claim 55, wherein, The specific surface area of ​​the pseudoboehmite is 200~320m². 2 / gr; average pore size is 5~50nm.

60. The low-VOC modified polypropylene composition according to any one of claims 1-46, wherein, The antioxidant is selected from one or more of hindered phenols, hindered amines, phosphites, and thiolated compounds.

61. The low-VOC modified polypropylene composition according to claim 60, wherein, The antioxidant is selected from at least one of pentaerythritol tetrakis[β-(3,5-di-tert-butyl-4-hydroxyphenyl)propionate], tris[2,4-di-tert-butylphenyl] phosphite, octadecyl β-(3,5-di-tert-butyl-4-hydroxyphenyl)propionate, 2,2'-methylenebis(4-methyl-6-tert-butylphenol), 2,2'-thiobis[3-(3,5-di-tert-butyl-4-hydroxyphenyl)propionate], 1,1,3-tris(2-methyl-4-hydroxy-5-tert-butylphenyl)butane and bis(2,4-di-tert-butylphenol) pentaerythritol diphosphite.

62. The low-VOC modified polypropylene composition according to any one of claims 1-46, wherein, The processing aid is selected from at least one of lubricants, acid absorbers, slip agents, antistatic agents, and anti-sticking agents; The lubricant is selected from at least one of the following: polyethylene glycol lubricants, fluoropolymer lubricants, organosilicon lubricants, fatty alcohol lubricants, fatty acid lubricants, fatty acid ester lubricants, stearamide lubricants, fatty acid metal soap lubricants, alkane and oxidized alkane lubricants, and micro / nanoparticle lubricants.

63. A biaxially oriented polypropylene film, wherein the biaxially oriented polypropylene film is prepared from the low-VOC modified polypropylene composition according to any one of claims 1-62.

64. The biaxially oriented polypropylene film according to claim 63, wherein, The biaxially oriented polypropylene film is prepared by a method comprising the following steps: (1) Mix and granulate the low-VOC modified polypropylene composition according to any one of claims 1-62; (2) The obtained granules are melt-extruded and cast into sheets to obtain modified polypropylene sheets; (3) The modified polypropylene casting is biaxially stretched to obtain the biaxially stretched polypropylene film.

65. The biaxially oriented polypropylene film according to claim 63 or 64, wherein, The biaxially oriented polypropylene film has a longitudinal tensile strength ≥130MPa; a transverse tensile strength ≥190MPa; a longitudinal elongation at break ≥210%; a transverse elongation at break ≥60%; a VOC content of less than 50μgC / g; and a thickness of 0.5~15 micrometers.

66. The biaxially oriented polypropylene film according to claim 65, wherein, The biaxially oriented polypropylene film has a longitudinal tensile strength of 140-170 MPa, a transverse tensile strength of 200-250 MPa, a longitudinal elongation at break of 225-280%, a transverse elongation at break of 62-90%, a VOC content of less than 45 μgC / g, and a thickness of 4-10 micrometers.

67. The biaxially oriented polypropylene film according to claim 66, wherein, The VOC content is less than 42 μgC / g.

68. The use of the biaxially oriented polypropylene film according to any one of claims 63-67 in the preparation of energy storage dielectrics.

69. The application according to claim 68, wherein, The energy storage medium is a high-temperature energy storage medium.

70. The application according to claim 68, wherein, The dielectric material is a single-layer / multi-layer capacitor film, roughening film, supercapacitor film, electrostatic film, or battery separator.

71. A green and environmentally friendly polypropylene capacitor film, wherein the polypropylene capacitor film is one or more layers, wherein at least one layer is the biaxially oriented polypropylene film as described in any one of claims 63-67.

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