MODIFIED FLEXIBLE POLYPROPYLENE INSULATING MATERIAL AND PREPARATION METHOD AND USE THEREOF

Description

TECHNICAL FIELD

The invention belongs to the field of insulating materials, in particular cable insulating materials, and particularly relates to a modified flexible polypropylene insulating material, a method for preparing the modified flexible polypropylene insulating material and use of the modified flexible polypropylene insulating material.

BACKGROUND ART

Polypropylene-based material has the advantages of natural high operating temperature and high breakdown field strength, has space charge inhibition characteristic and recyclable property, and is an optimal substitute for the existing cable insulating material—crosslinked polyethylene. However, as an insulating material, polypropylene is brittle and has insufficient toughness, and cannot meet the requirements of construction and layout of cables. Blending of polyolefin elastomer in polypropylene, or incorporation of low-modulus ethylene propylene copolymer into rubber phase is currently one of the main toughening means (see, e.g., EP893802A1, EP893801A1, KR1020180093807A, KR1020120095309A, etc.). However, this method inevitably leads to a decrease in the insulating property of the material, particularly the insulating property at high temperatures. Therefore, the insulating property of the material needs to be improved by means of additive, nano doping or graft modification and the like, to meet the working conditions of high temperature and high field strength of cables.

Graft modification is to introduce special functional groups on a polypropylene molecular chain, change molecular orbitals and introduce charge traps so as to improve the insulating property of the material. Compared with nano-particle doping modification, the method is featured with a simpler process, which solves the problem of unstable performance caused by nano-particle agglomeration, and has very high application potential.

CN105949394A discloses maleic anhydride grafted polypropylene material and preparation method thereof, the material having an obvious reduction in space charge accumulation after grafting. However, the melt grafting method adopted in the invention may seriously reduce the molecular weight of the material, so that the mechanical properties of the material cannot meet the actual requirements of cable insulating material.

US20140363671A1 discloses a cable using epoxy-containing group grafted polypropylene as an insulating material, but this patent discloses only a preparation method, and does not disclose structural parameters such as grafting ratio and the like of the material, nor the insulating property of the material.

CN111354507A mentions use of maleic anhydride grafted polypropylene as water tree inhibitor in cable insulating layer, however, the preparation and grafting ratio of the grafted polypropylene are not limited in detail, and the insulating property of the material is not disclosed either.

CONTENTS OF THE INVENTION

The invention aims to overcome the above defects of the prior art, and provide a modified flexible polypropylene insulating material which can give consideration to both mechanical property and electrical property at a higher working temperature, and is suitable for working conditions of high temperature and high operating field strength.

A first aspect of the invention is to provide a modified flexible polypropylene insulating material comprising a propylene-based continuous phase, and a rubber phase and a grafted phase derived from an unsaturated bond-containing polymerizable monomer dispersed in the propylene-based continuous phase; wherein, the modified flexible polypropylene insulating material has a content of xylene solubles of 10-55 wt %, preferably 15-45 wt %, more preferably 18-40 wt %, and still more preferably 20-40 wt %, based on the total weight of the modified flexible polypropylene insulating material; the content of structural units derived from the unsaturated bond-containing polymerizable monomer and in a grafted state in the modified flexible polypropylene insulating material is 0.3-6 wt %, and preferably 0.7-5 wt %; the flexural modulus of the modified flexible polypropylene insulating material is 200-1000 MPa, preferably 200-950 MPa, more preferably 200-700 MPa, and still more preferably 250-600 MPa; preferably, the ratio of the mass of the structural units derived from the unsaturated bond-containing polymerizable monomer in xylene insolubles to the mass of the structural units derived from the unsaturated bond-containing polymerizable monomer in the modified flexible polypropylene insulating material is more than 0.1, preferably 0.3-0.9.

A second aspect of the invention is to provide a method for preparing the above modified flexible polypropylene insulating material, comprising the following steps: blending modified polypropylene (A) and low-modulus polypropylene (B) to prepare the modified flexible polypropylene insulating material, wherein the modified polypropylene (A) is polypropylene graft-modified with a first unsaturated bond-containing polymerizable monomer, and the low-modulus polypropylene (B) is unmodified low-modulus polypropylene and/or low-modulus polypropylene graft-modified with a second unsaturated bond-containing polymerizable monomer; preferably, the first unsaturated bond-containing polymerizable monomer and the second unsaturated bond-containing polymerizable monomer are each independently an alkenyl-containing functional monomer and optionally an anhydride monomer.

A third aspect of the invention is to provide use of the above modified flexible polypropylene insulating material.

The modified flexible polypropylene insulating material of the invention can give consideration to both mechanical property and electrical property at a higher working temperature, and is suitable for working conditions of high temperature and high operating field strength. Compared with the polypropylene material obtained by alloying in a kettle, the polypropylene material mechanically blended with the low-modulus polypropylene results in products that have more diversity and regulation flexibility in structure, so that better performance can be obtained. Compared with the nano doping technology, the polymer graft-modified with an alkenyl-containing functional monomer introduced by dispersion can form a uniformly distributed nano dispersed phase, namely, an organic nanoparticle, in the composite material, so that the problems that inorganic nanoparticles are difficult to add and disperse and the like are solved. In addition, compared with the material in which small molecule additives are added, the graft-modified polypropylene material of the invention avoids performance reduction caused by small molecule migration, and therefore has better stability.

Additional features and advantages of the invention will be set forth in the detailed description of specific embodiments which follows.

BRIEF DESCRIPTION OF THE FIGURES

Exemplary embodiments of the invention will be described in more detail by referring to the figures.

FIG. 1 is an atomic force microscope photograph of the product of Example 1A in which the bright white portions indicated in the circles are the styrene grafted phase, the black portions are the rubber phase, and other portions are the continuous phase.

FIG. 2 is a photograph showing the microstructure of the product of Example 1A under an electron microscope at 10000 times, in which the spherical dispersed phase is the styrene grafted phase.

FIG. 3 is a photograph showing the microstructure of the product of Example 3A under an electron microscope at 10000 times.

FIG. 4 is a photograph showing the microstructure of the product of Example 4A under an electron microscope at 10000 times.

FIG. 5 is a photograph showing the microstructure of the product of Example 5A under an electron microscope at 10000 times.

FIG. 6 is a photograph showing the microstructure of the product of Comparative Example 3 under an electron microscope at 10000 times.

FIG. 7 is a photograph showing the microstructure of the product of Comparative Example 3 after etching under an electron microscope at 10000 times, wherein the black portions are the rubber phase.

FIG. 8 is a photograph showing the microstructure of the product of Comparative Example 4A under an electron microscope at 10000 times.

FIG. 9 is a photograph showing the microstructure of the product of Comparative Example 5A under an electron microscope at 10000 times.

FIG. 10 is an atomic force microscope photograph of the product of Example 1B in which the bright white portions indicated in the circles are the styrene-maleic anhydride grafted phase, the black portions are the rubber phase, and other portions are the continuous phase.

FIG. 11 is a photograph showing the microstructure of the product of Example 1B under an electron microscope at 20000 times, in which the spherical dispersed phase is the styrene-maleic anhydride grafted phase.

FIG. 12 is a photograph showing the microstructure of the product of Example 2B under an electron microscope at 20000 times.

FIG. 13 is a photograph showing the microstructure of the product of Example 3B under an electron microscope at 20000 times.

FIG. 14 is a photograph showing the microstructure of the product of Comparative Example 4B under an electron microscope at 20000 times.

FIG. 15 is a photograph showing the microstructure of the product of Comparative Example 5B under an electron microscope at 20000 times.

DETAILED DESCRIPTION OF THE INVENTION

The following is a detailed description of specific embodiments of the invention. It should be understood that the specific embodiments described herein are only to illustrate and explain, not to limit, the invention.

The invention provides a modified flexible polypropylene insulating material comprising a propylene-based continuous phase, and a rubber phase and a grafted phase derived from an unsaturated bond-containing polymerizable monomer dispersed in the propylene-based continuous phase; wherein, the modified flexible polypropylene insulating material has a content of xylene solubles of 10-55 wt %, preferably 15-45 wt %, more preferably 18-40 wt %, and still more preferably 20-40 wt %, based on the total weight of the modified flexible polypropylene insulating material; the content of structural units derived from the unsaturated bond-containing polymerizable monomer and in a grafted state in the modified flexible polypropylene insulating material is 0.3-6 wt %, preferably 0.7-5 wt %, and more preferably 0.4-4.5 wt %; the flexural modulus of the modified flexible polypropylene insulating material is 200-1000 MPa, preferably 200-950 MPa, more preferably 200-900 MPa, still more preferably 200-800 MPa, still more preferably 200-700 MPa, and still more preferably 250-600 MPa; preferably, the ratio of the mass of the structural units derived from the unsaturated bond-containing polymerizable monomer in xylene insolubles to the mass of the structural units derived from the unsaturated bond-containing polymerizable monomer in the modified flexible polypropylene insulating material is more than 0.1, preferably 0.3-0.9.

In one embodiment, the unsaturated bond-containing polymerizable monomer is an alkenyl-containing functional monomer; the content of structural units derived from the alkenyl-containing functional monomer and in a grafted state in the modified flexible polypropylene insulating material is 0.4-6 wt %, and preferably 1-5 wt %; the D50 of the grafted phase is less than 300 nm, preferably 10-250 nm, and more preferably 50-200 nm.

In another embodiment, the unsaturated bond-containing polymerizable monomer is an anhydride monomer and an alkenyl-containing functional monomer; the content of structural units derived from the anhydride monomer and the alkenyl-containing functional monomer and in a grafted state in the modified flexible polypropylene insulating material is 0.3-5 wt %, preferably 0.7-3 wt %, and the content of structural units derived from the anhydride monomer and in a grafted state is 0.05-2 wt %, preferably 0.2-0.5 wt %; the D50 of the grafted phase is less than 170 nm, preferably 10-150 nm, and more preferably 55-110 nm.

In the invention, the modified flexible polypropylene insulating material has a separated phase structure. Where the meaning of “continuous phase” is well known to those skilled in the art and refers to the matrix portion, the “rubber phase” refers to the soft xylene soluble portion, the “grafted phase” is formed from structural units derived from an unsaturated bond-containing polymerizable monomer, wherein the structural units derived from the unsaturated bond-containing polymerizable monomer may be wholly or predominantly derived from a grafted homo- or co-polypropylene, or may be partially derived from a grafted low-modulus polypropylene, and thus the structural units derived from the unsaturated bond-containing polymerizable monomer and “in a grafted state” refers to the structural units derived from the unsaturated bond-containing polymerizable monomer which form a covalent bond (graft) with the polypropylene and optionally the low-modulus polypropylene. The multiphase structure can be observed by an atomic force microscope, wherein the black portions observed by the atomic force microscope are the rubber phase, the bright white portions are the grafted phase, and other portions are the continuous phase. The grafted phase can also be directly observed by an electron microscope (the dispersed phase in the electron microscope image).

According to the invention, preferably, the modified flexible polypropylene insulating material has at least one of the following characteristics: the melt flow rate under the load of 2.16 kg at 230° C. is 0.5-15 g/10 min, preferably 0.6-10 g/10 min, and further preferably 0.8-6 g/10 min; the elongation at break is 200%, and preferably 300%; the tensile strength is more than 5 MPa, preferably 10-25 MPa.

In one embodiment, when the unsaturated bond-containing polymerizable monomer is an alkenyl-containing functional monomer, the modified flexible polypropylene insulating material has at least one of the following characteristics: the melt flow rate under the load of 2.16 kg at 230° C. is 0.5-15 g/10 min, preferably 0.6-10 g/10 min, and further preferably 0.8-6 g/10 min; the elongation at break is ≥200%, and preferably ≥300%; the tensile strength is more than 5 MPa, preferably 10-25 MPa.

In another embodiment, when the unsaturated bond-containing polymerizable monomer is an anhydride monomer and an alkenyl-containing functional monomer, the modified flexible polypropylene insulating material has at least one of the following characteristics: the melt flow rate under the load of 2.16 kg at 230° C. is 0.5-15 g/10 min, preferably 1-10 g/10 min, and further preferably 1.2-6 g/10 min; the elongation at break is ≥200%, and preferably ≥300%; the tensile strength is more than 5 MPa, preferably 10-25 MPa.

According to the invention, preferably, the modified flexible polypropylene insulating material has at least one of the following characteristics:

- the maximum working temperature of the modified flexible polypropylene insulating material is ≥90° C., preferably 100-160° C., and more preferably 110-140° C.;
- the breakdown field strength E_gat 110° C. of the modified flexible polypropylene insulating material is ≥285 kV/mm, preferably 290-800 kV/mm, and more preferably 300-750 kV/mm;
- the direct current volume resistivity ρ_vgat 110° C. and 40 kV/mm field strength of the modified flexible polypropylene insulating material is ≥1.0×10¹³Ω·m, preferably 1.5×10¹³Ω·m-1.0×10²⁰Ω·m;
- the dielectric constant at 110° C. and 50 Hz of the modified flexible polypropylene insulating material is greater than 2.0, and preferably 2.1-2.5.

- the maximum working temperature of the modified flexible polypropylene insulating material is ≥90° C., preferably 100-160° C., and more preferably 110-140° C.;
- the breakdown field strength E_gat 110° C. of the modified flexible polypropylene insulating material is ≥290 kV/mm, preferably 300-800 kV/mm, and more preferably 310-750 kV/mm; for example 320 kV/mm, 330 kV/mm, 340 kV/mm, 350 kV/mm, 400 kV/mm, 450 kV/mm, 500 kV/mm, 550 kV/mm, 600 kV/mm, 650 kV/mm, 700 kV/mm;
- the direct current volume resistivity ρ_vgat 110° C. and 40 kV/mm field strength of the modified flexible polypropylene insulating material is ≥1.0×10¹³Ω·m, preferably 1.5×10¹³Ω·m-1.0×10²⁰Ω·m;
- the dielectric constant at 110° C. and 50 Hz of the modified flexible polypropylene insulating material is greater than 2.0, and preferably 2.1-2.5.

- the maximum working temperature of the modified flexible polypropylene insulating material is ≥90° C., preferably 100-160° C., and more preferably 110-140° C.;
- the breakdown field strength E_gat 110° C. of the modified flexible polypropylene insulating material is 285 kV/mm, preferably 290-800 kV/mm, and more preferably 310-750 kV/mm; for example 320 kV/mm, 330 kV/mm, 340 kV/mm, 350 kV/mm, 400 kV/mm, 450 kV/mm, 500 kV/mm, 550 kV/mm, 600 kV/mm, 650 kV/mm, 700 kV/mm;
- the direct current volume resistivity ρ_vgat 110° C. and 40 kV/mm field strength of the modified flexible polypropylene insulating material is 2.0×10¹³Ω·m, preferably 4.0×10¹³Ω·m-1.0×10²⁰Ω·m;
- the dielectric constant at 110° C. and 50 Hz of the modified flexible polypropylene insulating material is greater than 2.0, and preferably 2.1-2.5.

The maximum working temperature is defined as the working temperature at which the material can be used stably for a long period of time, as is well known in the art. The above excellent insulating properties obtained by the material of the invention tested at 110° C. can prove that the material of the invention has the maximum working temperature of at least 110° C.

Grafting modification of polypropylene by alkenyl-containing functional monomer can significantly improve the breakdown strength of the material with simple raw materials; on this basis, the addition of an anhydride monomer for copolymerization can achieve a more significant resistivity improvement effect at a smaller total monomer addition. In addition, the grafting with an anhydride monomer can also effectively improve the water tree resistance of the insulating material.

According to the invention, the anhydride monomer may be selected from anhydrides having at least one alkenyl group; preferably, the anhydride monomer is selected from maleic anhydride and/or itaconic anhydride; further preferably, the anhydride monomer is maleic anhydride.

The alkenyl groups in the alkenyl-containing functional monomer of the invention are used for grafting with polypropylene/low-modulus polypropylene, and therefore, alkenyl-containing functional monomers having reactable alkenyl groups are all suitable for use in the invention.

Specifically, the alkenyl-containing functional monomer is selected from at least one of monomers having a structure represented by the formula 1,

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in the formula 1, R_b, R_c, R_dare each independently selected from H, substituted or unsubstituted alkyl; R_ais selected from substituted or unsubstituted alkyl, substituted or unsubstituted alkoxy, substituted or unsubstituted aryl, substituted or unsubstituted ester group, substituted or unsubstituted carboxyl, substituted or unsubstituted cycloalkyl or heterocyclyl, cyano, substituted or unsubstituted silyl.

According to a preferred embodiment of the invention, R_b, R_c, R_dare each independently selected from H, substituted or unsubstituted C₁-C₆alkyl; R_ais selected from substituted or unsubstituted C₁-C₂₀alkyl, substituted or unsubstituted C₁-C₂₀alkoxy, substituted or unsubstituted C₆-C₂₀aryl, substituted or unsubstituted C₁-C₂₀ester group, substituted or unsubstituted C₁-C₂₀carboxyl, substituted or unsubstituted C₃-C₂₀cycloalkyl or heterocyclyl, cyano, substituted or unsubstituted C₃-C₂₀silyl; the substituent group is halogen, hydroxy, amino, C₁-C₁₂alkyl, C₃-C₆cycloalkyl, C₁-C₁₂alkoxy, C₁-C₁₂acyloxy.

According to a more preferred embodiment of the invention, wherein, R_b, R_c, R_dare each independently selected from H, substituted or unsubstituted C₁-C₆alkyl;

R_ais selected from a group represented by formula 2, a group represented by formula 3, a group represented by formula 4, a group represented by formula 5, a group represented by formula 6, a combination of a group represented by formula 6 and a group represented by formula 7, a heterocyclic group;

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- in the formula 2, R⁴-R⁸are each independently selected from H, halogen, hydroxy, amino, phosphoric group, sulfonic group, substituted or unsubstituted C₁-C₁₂alkyl, substituted or unsubstituted C₃-C₁₂cycloalkyl, substituted or unsubstituted C₁-C₁₂alkoxy, substituted or unsubstituted C₁-C₁₂ester group, substituted or unsubstituted C₁-C₁₂amino, the substituent group is selected from halogen, hydroxy, amino, phosphoric group, sulfonic group, C₁-C₁₂alkyl, C₃-C₁₂cycloalkyl, C₁-C₁₂alkoxy, C₁-C₁₂ester group, C₁-C₁₂amino; preferably, R⁴-R⁸are each independently selected from H, halogen, hydroxy, amino, substituted or unsubstituted C₁-C₆alkyl, substituted or unsubstituted C₁-C₆alkoxy;

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- in the formula 3, R₄-R₁₀are each independently selected from H, halogen, hydroxy, amino, phosphoric group, sulfonic group, substituted or unsubstituted C₁-C₁₂alkyl, substituted or unsubstituted C₃-C₁₂cycloalkyl, substituted or unsubstituted C₁-C₁₂alkoxy, substituted or unsubstituted C₁-C₁₂ester group, substituted or unsubstituted C₁-C₁₂amino, the substituent group is selected from halogen, hydroxy, amino, phosphoric group, sulfonic group, C₁-C₁₂alkyl, C₃-C₁₂cycloalkyl, C₁-C₁₂alkoxy, C₁-C₁₂ester group, C₁-C₁₂amino; preferably, R₄-R₁₀are each independently selected from H, halogen, hydroxy, amino, substituted or unsubstituted C₁-C₆alkyl, substituted or unsubstituted C₁-C₆alkoxy, the substituent group is selected from halogen, hydroxy, amino, C₁-C₆alkyl, C₁-C₆alkoxy;

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- in the formula 4, R₄′-R₁₀′ are each independently selected from H, halogen, hydroxy, amino, phosphoric group, sulfonic group, substituted or unsubstituted C₁-C₁₂alkyl, substituted or unsubstituted C₃-C₁₂cycloalkyl, substituted or unsubstituted C₁-C₁₂alkoxy, substituted or unsubstituted C₁-C₁₂ester group, substituted or unsubstituted C₁-C₁₂amino, the substituent group is selected from halogen, hydroxy, amino, phosphoric group, sulfonic group, C₁-C₁₂alkyl, C₃-C₁₂cycloalkyl, C₁-C₁₂alkoxy, C₁-C₁₂ester group, C₁-C₁₂amino; preferably, R₄′-R₁₀′ are each independently selected from H, halogen, hydroxy, amino, substituted or unsubstituted C₁-C₆alkyl, substituted or unsubstituted C₁-C₆alkoxy, the substituent group is selected from halogen, hydroxy, amino, C₁-C₆alkyl, C₁-C₆alkoxy;

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- in the formula 5, R′, R″, R′″ are each independently selected from substituted or unsubstituted C₁-C₁₂linear alkyl, substituted or unsubstituted C₃-C₁₂branched alkyl, substituted or unsubstituted C₁-C₁₂alkoxy, substituted or unsubstituted C₁-C₁₂acyloxy; preferably, R₁is C₂-C₆alkenyl, preferably monounsaturated alkenyl; R₂, R₃, R₄are each independently selected from substituted or unsubstituted C₁-C₆linear alkyl, substituted or unsubstituted C₃-C₆branched alkyl, substituted or unsubstituted C₁-C₆alkoxy, substituted or unsubstituted C₁-C₆acyloxy;

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- in the formula 6, R_mis selected from the following groups that are substituted or unsubstituted: C₁-C₂₀linear alkyl, C₃-C₂₀branched alkyl, C₃-C₁₂cycloalkyl, C₃-C₁₂epoxyalkyl, C₃-C₁₂epoxyalkylalkyl, the substituent group is selected from at least one of halogen, amino and hydroxy;
- the heterocyclic group is selected from imidazolyl, pyrazolyl, carbazolyl, pyrrolidinonyl, pyridyl, piperidinyl, caprolactanyl, pyrazinyl, thiazolyl, purinyl, morpholinyl, oxazolinyl.

In one embodiment, when the unsaturated bond-containing polymerizable monomer is an alkenyl-containing functional monomer, preferably, R_ais selected from a group represented by the formula 2, a group represented by the formula 3, a group represented by the formula 4, a group represented by the formula 5, a group represented by the formula 6, a combination of a group represented by the formula 6 and a group represented by the formula 7, a heterocyclic group.

In another embodiment, when the unsaturated bond-containing polymerizable monomer is an anhydride monomer and an alkenyl-containing functional monomer, preferably, R_ais selected from a group represented by the formula 2, a group represented by the formula 3, a group represented by the formula 4, a group represented by the formula 6, a combination of a group represented by the formula 6 and a group represented by the formula 7, a heterocyclic group.

According to a specific embodiment of the invention, the alkenyl-containing functional monomer is an aromatic olefin monomer, the aromatic olefin monomer is selected from at least one of styrene, α-methylstyrene, 1-vinyl naphthalene, 2-vinyl naphthalene, mono- or polysubstituted styrene, mono- or polysubstituted α-methylstyrene, mono- or polysubstituted 1-vinyl naphthalene and mono- or polysubstituted 2-vinyl naphthalene; the substituent group preferably is selected from at least one of halogen, hydroxy, amino, phosphoric group, sulfonic group, C₁-C₈linear alkyl, C₃-C₈branched alkyl or cycloalkyl, C₁-C₆linear alkoxy, C₃-C₈branched alkoxy or cycloalkoxy, C₁-C₈linear ester group, C₃-C₈branched ester group or cyclic ester group, C₁-C₈linear amine group and C₃-C₈branched amine group or cyclic amine group; preferably, the aromatic olefin monomer is selected from at least one of styrene, α-methylstyrene, 2-methylstyrene, 3-methylstyrene and 4-methylstyrene.

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

According to a specific embodiment of the invention, the alkenyl-containing functional monomer is an acrylate monomer and an optional acrylic monomer, preferably, the acrylate monomer is selected from at least one of methyl (methyl)acrylate, sec-butyl (methyl)acrylate, ethyl (methyl)acrylate, n-butyl (methyl)acrylate, isobutyl (methyl)acrylate, tert-butyl (methyl)acrylate, isooctyl (methyl)acrylate, dodecyl (methyl)acrylate, cocinin (methyl)acrylate, octadecyl (methyl)acrylate, dimethylaminoethyl (methyl)acrylate, diethylaminoethyl (methyl)acrylate, dimethylaminopropyl (methyl)acrylate, and glycidyl (methyl)acrylate. Preferably, the acrylic monomer is selected from at least one of acrylic acid, methacrylic acid and 2-ethylacrylic acid.

In the invention, the C₃-C₁₂epoxyalkylalkyl refers to epoxyalkyl-substituted alkyl having 3 to 12 carbon atoms, e.g., oxiranylmethyl.

In the invention, the structural units derived from the acrylic monomer may be absent or may be present together with the structural units derived from the acrylate monomer, preferably, the molar ratio of the structural units derived from the acrylate monomer to the structural units derived from the acrylic monomer is 1: 0-2, preferably 1:0.125-1.

According to a specific embodiment of the invention, the alkenyl-containing functional monomer is an alkenyl-containing heterocyclic monomer. The alkenyl-containing heterocyclic monomer of the invention may be any alkenyl-containing heterocyclic compound capable of undergoing radical polymerization, which may be selected from at least one of alkenyl-containing imidazoles, alkenyl-containing pyrazoles, alkenyl-containing carbazoles, alkenyl-containing pyrrolidones, alkenyl-containing pyridines or pyridiniums, alkenyl-containing piperidines, alkenyl-containing caprolactams, alkenyl-containing pyrazines, alkenyl-containing thiazoles, alkenyl-containing purines, alkenyl-containing morpholines and alkenyl-containing oxazolines; preferably, the alkenyl-containing heterocyclic monomer is a monoalkenyl-containing heterocyclic monomer.

Specifically, the alkenyl-containing heterocyclic monomer is selected from: at least one of 1-vinyl imidazole, 2-methyl-1-vinyl imidazole, N-allyl imidazole, 1-vinyl pyrazole, 3-methyl-1-vinyl pyrazole, vinyl carbazole, N-vinyl pyrrolidone, 2-vinyl pyridine, 3-vinyl pyridine, 4-vinyl pyridine, 2-methyl-5-vinyl pyridine, vinyl pyridine N oxide, vinyl pyridinium, vinyl piperidine, N-vinyl caprolactam, 2-vinyl pyrazine, N-vinyl piperazine, 4-methyl-5-vinyl thiazole, N-vinyl purine, vinyl morpholine and vinyl oxazoline.

Further, the alkenyl-containing polymerizable monomer is selected from at least one of vinyl acetate, styrene, α-methylstyrene, (meth)acrylate, vinyl alkyl ether, vinyl pyrrolidone, vinyl pyridine, vinyl imidazole and acrylonitrile; the (meth)acrylate is preferably selected from at least one of methyl (meth)acrylate, ethyl (meth)acrylate, and glycidyl (meth)acrylate; preferably, the alkenyl-containing polymerizable monomer is selected from vinyl acetate, styrene, α-methylstyrene; further preferably, the alkenyl-containing polymerizable monomer is styrene.

According to the invention, preferably, the modified flexible polypropylene insulating material comprises modified polypropylene (A) which is polypropylene graft-modified with a first unsaturated bond-containing polymerizable monomer, and low-modulus polypropylene (B) which is unmodified low-modulus polypropylene and/or low-modulus polypropylene graft-modified with a second unsaturated bond-containing polymerizable monomer;

- preferably, the first unsaturated bond-containing polymerizable monomer and the second unsaturated bond-containing polymerizable monomer are each independently an alkenyl-containing functional monomer and optionally an anhydride monomer;
- preferably, the content of the modified polypropylene (A) is 20-80 wt %, preferably 30-70 wt %, and more preferably 35-65 wt %, and the content of the low-modulus polypropylene (B) is 20-80 wt %, preferably 30-70 wt %, and more preferably 35-65 wt %, based on the total weight of the modified flexible polypropylene insulating material.

In one embodiment, the modified flexible polypropylene insulating material comprises a polypropylene (A) graft-modified with an alkenyl-containing functional monomer, and a low-modulus polypropylene (B) which is unmodified low-modulus polypropylene and/or low-modulus polypropylene graft-modified with an alkenyl-containing functional monomer.

In another embodiment, the modified flexible polypropylene insulating material comprises a modified polypropylene (A) which is a polypropylene graft-modified with an alkenyl-containing functional monomer and optionally graft-modified with an anhydride monomer, and a low-modulus polypropylene (B) which is an unmodified low-modulus polypropylene and/or a low-modulus polypropylene graft-modified with an alkenyl-containing functional monomer and optionally graft-modified with an anhydride monomer. That is, the modified polypropylene (A) may be a polypropylene graft-modified with an alkenyl-containing functional monomer, or a polypropylene graft-modified with dual monomers comprising an alkenyl-containing functional monomer and an anhydride monomer, and the low-modulus polypropylene (B) may be an unmodified low-modulus polypropylene, or a low-modulus polypropylene graft-modified with an alkenyl-containing functional monomer, or a low-modulus polypropylene graft-modified with dual monomers comprising an alkenyl-containing functional monomer and an anhydride monomer, or a mixture thereof. When the modified polypropylene (A) is a polypropylene graft-modified with an alkenyl-containing functional monomer, the low-modulus polypropylene (B) must be a low-modulus polypropylene graft-modified with dual monomers comprising an alkenyl-containing functional monomer and an anhydride monomer. When the modified polypropylene (A) is a polypropylene graft-modified with dual monomers comprising an alkenyl-containing functional monomer and an anhydride monomer, the low-modulus polypropylene (B) may be an unmodified low-modulus polypropylene, a low-modulus polypropylene graft-modified with an alkenyl-containing functional monomer, or a low-modulus polypropylene graft-modified with dual monomers comprising an alkenyl-containing functional monomer and an anhydride monomer. The invention has no special requirements for the grafting component content of each raw material, as long as the total grafting amount of the above modified flexible polypropylene insulating material is satisfied.

In the three-phase structure of the modified flexible polypropylene insulating material of the present invention, the graft-modified polypropylene (A) at least provides a propylene-based continuous phase and a grafted phase; the low-modulus polypropylene (B) provides a propylene-based continuous phase and a rubber phase, and optionally a grafted phase.

According to the invention, the modified flexible polypropylene insulating material can be prepared by blending the modified polypropylene (A) with the low-modulus polypropylene (B).

In the invention, the modified polypropylene (A) comprises structural units derived from homo- or co-polypropylene and structural units derived from an unsaturated bond-containing polymerizable monomer; the content of the structural units derived from the unsaturated bond-containing polymerizable monomer and in a grafted state in the modified polypropylene (A) is 0.1-20 wt %, preferably 1-15 wt %, based on the weight of the modified polypropylene (A).

In one embodiment, the modified polypropylene (A) comprises structural units derived from homo- or co-polypropylene and structural units derived from an alkenyl-containing functional monomer; the content of the structural units derived from the alkenyl-containing functional monomer and in a grafted state in the modified polypropylene (A) is 0.5-20 wt %, preferably 1-15 wt %, based on the weight of the modified polypropylene (A).

In another embodiment, the modified polypropylene (A) comprises structural units derived from homo- or co-polypropylene, and structural units derived from an alkenyl-containing functional monomer and optionally structural units derived from an anhydride monomer; the content of the structural units in a grafted state in the modified polypropylene (A) is 0.1-10 wt %, preferably 1-5 wt %, based on the weight of the modified polypropylene (A).

The term “structural unit” means that it is a part of the modified polypropylene (A), and the form thereof is not limited. Specifically, the term “structural units derived from homo- or co-polypropylene” refers to products formed from homo- or co-polypropylene, including not only those in “group” form but also those in “polymer” form. The term “structural units derived from an unsaturated bond-containing polymerizable monomer” refers to products formed from an unsaturated bond-containing polymerizable monomer, including not only those in “group” form, but also those in “monomer” form, as well those in “polymer” form. The term “structural units derived from an alkenyl-containing functional monomer” refers to products formed from an alkenyl-containing functional monomer, including not only those in “group” form, but also those in “monomer” form, as well those in “polymer” form. The term “structural units derived from a (maleic) anhydride monomer” refers to products formed from a (maleic) anhydride monomer, including not only those in “group” form, but also those in “monomer” form, as well those in “polymer” form. Said “structural unit” may be a repeating unit or a non-repeating independent unit.

In the invention, the term “comonomer” of the polypropylene copolymer is known to those of ordinary skill in the art, and means a monomer copolymerized with propylene.

According to a preferred embodiment of the invention, the homo- or co-polypropylene has at least one of the following characteristics: the comonomer content is 0-15 mol %, preferably 0-12 mol %, more preferably 0-8 mol %; the melt flow rate under a load of 2.16 kg at 230° C. is 1-10 g/10 min, preferably 2-5 g/10 min; the melting temperature Tm is 110-180° C., further preferably 120-170° C.; the weight average molecular weight is 20×10⁴-50×10⁴g/mol; the flexural modulus is 500-2000 MPa, preferably 600-1700 MPa; the elongation at break is 200%, preferably 300%, the tensile strength is greater than 5 MPa, preferably 10-40 MPa; the content of xylene solubles is less than 15 wt %, preferably 0.5-8 wt %.

According to a preferred embodiment of the invention, the comonomer of the co-polypropylene is selected from at least one of C₂-C₈α-olefins (ethylene is considered herein to be α-olefin) other than propylene; the comonomer of the co-polypropylene is selected from at least one of ethylene and C₄-C₈α-olefin; preferably, the comonomer of the co-polypropylene is selected from at least one of ethylene, 1-butene, 1-pentene, 4-methyl-1-pentene, 1-hexene, 1-heptene and 1-octene; further preferably, the comonomer of the co-polypropylene is ethylene and/or 1-butene; the comonomer content is 0.1-15 mol %, preferably 0.1-12 mol %, and more preferably 0.1-8 mol %, based on the total molar amount of the monomers. The co-polypropylene of the invention is preferably a porous granular or powdery resin.

The homo- or co-polypropylene of the invention can be any commercially available polypropylene powder suitable for the invention, and can also be produced by the polymerization processes recited in the Chinese patents CN102453180B, CN101490096B, CN102816269B, CN102816270B and the like.

The term “low-modulus polypropylene” according to the invention is well known to those skilled in the art and is preferably a copolymer of propylene with ethylene or a higher alpha-olefin (preferably C₄-C₈alpha-olefin), preferably an ethylene-propylene copolymer, having a flexural modulus of less than 300 MPa; specifically, the copolymer of propylene with ethylene or a higher alpha-olefin comprises a propylene homopolymer and/or propylene random copolymer matrix component (1) as a matrix phase and, dispersed therein, as a dispersed phase, another propylene copolymer component (2) comprising one or more ethylene or higher alpha-olefin (preferably C₄-C₈alpha-olefin) comonomers. In the propylene random copolymer, the comonomers are randomly distributed in the main chain of the propylene polymer. Preferably, the propylene copolymer (2) dispersed in the homopolymer or copolymer matrix (1) of the low-modulus polypropylene is substantially amorphous. The term “substantially amorphous” means herein that the propylene copolymer (2) has a lower crystallinity than the homopolymer or copolymer matrix (1).

The low-modulus polypropylene may be of sea-island structure or co-continuous structure. Preferably, the low-modulus polypropylene of the invention is a heterophasic propylene copolymer prepared in situ in a reactor according to existing processes.

According to the invention, preferably, the low-modulus polypropylene has at least one of the following characteristics: the comonomer content is 8-25 wt %, preferably 10-22 wt %; the content of xylene solubles is 18-75 wt %, preferably 30-70 wt %, and more preferably 30-67 wt %; the melt flow rate under a load of 2.16 kg at 230° C. is 0.1-15 g/10 min, preferably 0.2-7 g/10 min; the melting temperature Tm is 120-165° C., and further preferably 125-150° C.; the flexural modulus is 10-300 MPa, preferably 15-250 MPa; the comonomer content in the xylene solubles is 10-50 wt %, preferably 20-35 wt %; the intrinsic viscosity ratio of the xylene solubles to the low-modulus polypropylene is 0.5-3, preferably 0.8-1.3; the weight average molecular weight is 25×10⁴-70×10⁴g/mol.

The low-modulus polypropylene described in the invention includes, but is not limited to, any commercially available polypropylene powder and pellets suitable for the invention, and can also be produced by the polymerization processes recited in the Chinese patents CN1069908C, CN1049932C, CN1108315C, CN1117610C, CN1132865C, CN102020733B, and the like. Common polymerization processes include Spheripol process from Basell, Hypol process from Mitsui oil chemical, Borstar PP process from Borealis, Unipol process from DOW chemical, Innovene gas phase process from INEOS (original BP-Amoco), and the like.

In the invention, the term “low-modulus polypropylene” generally refers to ungrafted (i.e., unmodified) low-modulus polypropylene when grafting is not specified.

According to the invention, the content of the structural units in a grafted state in the low-modulus polypropylene (B) is 0-5 wt %, preferably 0.2-2.5 wt %, based on the weight of the low-modulus polypropylene (B).

In one embodiment, when the low-modulus polypropylene (B) is a low-modulus polypropylene graft-modified with an alkenyl-containing functional monomer, the content of the structural units derived from the alkenyl-containing functional monomer and is in a grafted state in the low-modulus polypropylene graft-modified with the alkenyl-containing functional monomer is 0.1-5 wt %, preferably 0.2-2.5 wt %, based on the weight of the low-modulus polypropylene graft-modified with the alkenyl-containing functional monomer.

In another embodiment, when the low-modulus polypropylene (B) is a low-modulus polypropylene graft-modified with an alkenyl-containing functional monomer and an anhydride monomer, the content of the structural units in a grafted state in the low-modulus polypropylene graft-modified with the alkenyl-containing functional monomer and the anhydride monomer is 0.1-5 wt %, preferably 0.5-2.5 wt %, based on the weight of the low-modulus polypropylene graft-modified with the alkenyl-containing functional monomer and the anhydride monomer.

The invention also provides a method for preparing the modified flexible polypropylene insulating material, which comprises the following steps: blending modified polypropylene (A) and low-modulus polypropylene (B) to prepare the modified flexible polypropylene insulating material, wherein the modified polypropylene (A) is polypropylene graft-modified with a first unsaturated bond-containing polymerizable monomer, and the low-modulus polypropylene (B) is unmodified low-modulus polypropylene and/or low-modulus polypropylene graft-modified with a second unsaturated bond-containing polymerizable monomer.

Preferably, the first unsaturated bond-containing polymerizable monomer and the second unsaturated bond-containing polymerizable monomer are each independently an alkenyl-containing functional monomer and optionally an anhydride monomer.

Preferably, the content of the modified polypropylene (A) is 20-80 wt %, preferably 30-70 wt %, and more preferably 35-65 wt %, and the content of the low-modulus polypropylene (B) is 20-80 wt %, preferably 30-70 wt %, and more preferably 35-65 wt %, based on the total weight of the modified flexible polypropylene insulating material.

According to a preferred embodiment of the invention, the preparation method comprises the following steps:

S1: subjecting a reaction mixture A comprising homo- or co-polypropylene and a first unsaturated bond-containing polymerizable monomer to grafting reaction in the presence of an inert gas, to obtain a modified polypropylene; optionally, subjecting a reaction mixture B comprising a low-modulus polypropylene and a second unsaturated bond-containing polymerizable monomer to grafting reaction in the presence of an inert gas, to obtain a modified low-modulus polypropylene;

S2: mixing the modified polypropylene with an unmodified low-modulus polypropylene and/or the modified low-modulus polypropylene and optional additives, and extruding and granulating to obtain the modified flexible polypropylene insulating material.

Preferably, the grafting sites are initiated by a free radical initiator and the grafting reaction proceeds further. In this case, the reaction mixture A and the reaction mixture B also each independently comprise a free radical initiator.

Wherein, the peroxide-based radical initiator is preferably selected from at least one of dibenzoyl peroxide, dicumyl peroxide, di-tert-butyl peroxide, lauroyl peroxide, dodecyl peroxide, tert-butyl peroxybenzoate, diisopropyl peroxydicarbonate, tert-butyl peroxy (2-ethylhexanoate) and dicyclohexyl peroxydicarbonate; the azo-based radical initiator is preferably azobisisobutyronitrile and/or azobisisoheptonitrile.

More preferably, the grafting sites are initiated by a peroxide-based free radical initiator and the grafting reaction proceeds further.

Furthermore, the grafting reaction of the invention can also be carried out according to the methods described in CN106543369A, CN104499281A, CN102108112A, CN109251270A, CN1884326A and CN 101492517B.

The amount of each component used in the grafting reaction of the invention is not particularly limited on the premise that the above-mentioned product characteristics are satisfied, and specifically, the ratio of the mass of the radical initiator to the total mass of the unsaturated bond-containing polymerizable monomers is 0.01-10:100, preferably 0.5-6:100. The mass ratio of the first unsaturated bond-containing polymerizable monomer to the homo- or co-polypropylene is 0.5-35:100, preferably 2-30:100, and more preferably 2.5-25:100. The mass ratio of the second unsaturated bond-containing polymerizable monomer to the low-modulus polypropylene is 0.1-20:100, preferably 0.2-15:100, and more preferably 0.5-10:100.

In one embodiment, when both the first unsaturated bond-containing polymerizable monomer and the second unsaturated bond-containing polymerizable monomer are alkenyl-containing functional monomers, the mass ratio of the radical initiator to the alkenyl-containing functional monomers is 0.01-10:100, preferably 0.5-5:100. The mass ratio of the alkenyl-containing functional monomers to the homo- or co-polypropylene is 0.5-35:100, preferably 2-30:100, and further preferably 5-25:100; the mass ratio of the alkenyl-containing functional monomers to the low-modulus polypropylene is 0.1-20:100, preferably 0.2-10:100, and more preferably 0.5-5:100.

In another embodiment, when the first unsaturated bond-containing polymerizable monomer and/or the second unsaturated bond-containing polymerizable monomer include an alkenyl-containing functional monomer and an anhydride monomer, the ratio of the mass of the radical initiator to the total mass of the unsaturated bond-containing polymerizable monomers in the reaction system may be 0.1-10:100, preferably 0.5-6:100. The mass ratio of the total mass of the first unsaturated bond-containing polymerizable monomer to the homo- or co-polypropylene may be 0.5-35:100, preferably 2-30:100, and more preferably 2.5-20:100; the mass ratio of the total mass of the second unsaturated bond-containing polymerizable monomer to the low-modulus polypropylene may be 0.5-15:100, preferably 2-10:100; when the unsaturated bond-containing polymerizable monomer includes an alkenyl-containing functional monomer and an anhydride monomer, the mass ratio of the alkenyl-containing functional monomer to the anhydride monomer may be 0.5-10:1, preferably 2-8:1.

The invention also has no special limitation on the technical conditions of the grafting reaction, preferably, the grafting reaction is a solid phase grafting reaction. Specifically, the temperature of the grafting reaction is 30-130° C., and preferably 60-120° C.; the time is 0.5-10 h, and preferably 1-6 h.

In the invention, the term “reaction mixture” includes all materials added to the grafting reaction system, and the materials may be added at one time or at different stages of the reaction.

The reaction mixture A and the reaction mixture B of the invention may also each independently comprise a dispersant, wherein the dispersant is preferably water or an aqueous solution of sodium chloride. The mass content of the dispersant is preferably 50-300% of the mass of the polypropylene.

The reaction mixture A and the reaction mixture B of the invention may further each independently comprise an interfacial agent, wherein the interfacial agent is an organic solvent having a swelling effect on polyolefin, and is preferably at least one of the following organic solvents having a swelling effect on polypropylene: ether solvents, ketone solvents, aromatic hydrocarbon solvents, and alkane solvents; more preferably at least one of the following organic solvents: chlorobenzene, polychlorinated benzene, alkanes or cycloalkanes of C₆or more, benzene, C₁-C₄alkyl substituted benzene, C₂-C₆fatty ethers, C₃-C₆fatty ketones and decalin; further preferably at least one of the following organic solvents: benzene, toluene, xylene, chlorobenzene, tetrahydrofuran, diethyl ether, acetone, hexane, cyclohexane, decalin, heptane. The mass content of the interfacial agent is preferably 1-30%, and more preferably 10-25%, of the mass of the polypropylene.

The reaction mixture A and the reaction mixture B of the invention may further each independently comprise an organic solvent as a solvent for dissolving the solid radical initiator, the organic solvent preferably comprising at least one of C₂-C₅alcohols, C₂-C₄ethers and C₃-C₅ketones, more preferably comprising at least one of C₂-C₄alcohols, C₂-C₃ethers and C₃-C₅ketones, and most preferably 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.

According to a preferred embodiment of the invention, the preparation method comprises the following steps:

- a. placing a homo- or co-polypropylene in a closed reactor, followed by inert gas replacement;
- b. adding a free radical initiator and a first unsaturated bond-containing polymerizable monomer to the closed reactor, and mixing with stirring;
- c. optionally adding an interfacial agent and optionally swelling the reaction system;
- d. optionally adding a dispersant, and heating the reaction system to the grafting reaction temperature, to carry out the grafting reaction;
- e. after the end of the reaction, optionally filtering (in the case of using an aqueous phase dispersant), drying to obtain a modified polypropylene;
- f. mixing the modified polypropylene with ungrafted and/or grafted low-modulus polypropylene and optional aids, melt extruding and granulating, to obtain the modified flexible polypropylene insulating material;
- wherein, the preparation method of the grafted low-modulus polypropylene comprises the following steps:
- i. placing a low-modulus polypropylene in a closed reactor, followed by inert gas replacement;
- ii. adding a free radical initiator and a second unsaturated bond-containing polymerizable monomer to the closed reactor, and mixing with stirring;
- iii. optionally adding an interfacial agent and optionally swelling the reaction system;
- iv. optionally adding a dispersant, and heating the reaction system to the grafting reaction temperature, to carry out the grafting reaction;
- v. after the end of the reaction, optionally filtering (in the case of using an aqueous phase dispersant), drying to obtain a modified low-modulus polypropylene.

Specifically, the preparation method comprises the following steps:

- a. placing a homo- or co-polypropylene in a closed reactor, followed by inert gas replacement;
- b. adding a free radical initiator and a first unsaturated bond-containing polymerizable monomer to the closed reactor, and mixing with stirring;
- c. adding 0-30 parts of an interfacial agent, and optionally swelling the reaction system at 20-60° C. for 0-24 h;
- d. adding 0-300 parts of a dispersant, and heating the system to the graft polymerization temperature of 30-130° C., to carry out the reaction for 0.5-10 h;
- e. after the end of the reaction, optionally filtering (in the case of using an aqueous phase dispersant), drying to obtain a modified polypropylene;
- f. weighing the modified polypropylene and ungrafted and/or grafted low-modulus polypropylene and optional aids in proportions, mixing and granulating by using a twin-screw extruder at a melting temperature of 180-230° C. and a screw speed of 30-600 rpm, to obtain the modified flexible polypropylene insulating material;
- wherein, the preparation method of the grafted low-modulus polypropylene comprises the following steps:
- i. placing a low-modulus polypropylene in a closed reactor, followed by inert gas replacement;
- ii. adding a free radical initiator and a second unsaturated bond-containing polymerizable monomer to the closed reactor, and mixing with stirring;
- iii. adding 0-30 parts of an interfacial agent, and optionally swelling the reaction system at 20-60° C. for 0-24 h;
- iv. adding 0-300 parts of a dispersant, and heating the system to the graft polymerization temperature of 30-130° C., to carry out the reaction for 0.5-10 h;
- v. after the end of the reaction, optionally filtering (in the case of using an aqueous phase dispersant), drying to obtain a modified low-modulus polypropylene.

According to another preferred embodiment of the invention, the preparation method comprises the following steps:

- a. placing a homo- or co-polypropylene in a closed reactor, followed by inert gas replacement;
- b. mixing an organic solvent and a free radical initiator, and adding the mixture to the closed reactor;
- c. removing the organic solvent;
- d. adding a first unsaturated bond-containing polymerizable monomer, optionally adding an interfacial agent, and optionally swelling the reaction system;
- e. optionally adding a dispersant, and heating the reaction system to the grafting reaction temperature, to carry out the grafting reaction;
- f. after the end of the reaction, optionally filtering (in the case of using an aqueous phase dispersant), drying to obtain a modified polypropylene;
- g. weighing the modified polypropylene and ungrafted and/or grafted low-modulus polypropylene and optional aids in proportions, mixing, melt extruding and granulating, to obtain the modified flexible polypropylene insulating material;
- wherein, the preparation method of the grafted low-modulus polypropylene comprises the following steps:
- i. placing a low-modulus polypropylene in a closed reactor, followed by inert gas replacement;
- ii. mixing an organic solvent and a free radical initiator, and adding the mixture to the closed reactor;
- iii. removing the organic solvent;
- iv. adding a second unsaturated bond-containing polymerizable monomer, optionally adding an interfacial agent, and optionally swelling the reaction system;
- v. optionally adding a dispersant, and heating the reaction system to the grafting reaction temperature, to carry out the grafting reaction;
- vi. after the end of the reaction, optionally filtering (in the case of using an aqueous phase dispersant), drying to obtain a modified low-modulus polypropylene.

Specifically, the preparation method comprises the following steps:

- a. placing a homo- or co-polypropylene in a closed reactor, followed by inert gas replacement;
- b. mixing an organic solvent and a free radical initiator, and adding the mixture to the closed reactor;
- c. removing the organic solvent;
- d. adding a first unsaturated bond-containing polymerizable monomer, adding 0-30 parts of an interfacial agent, and optionally swelling the reaction system at 20-60° C. for 0-24 h;
- e. adding 0-300 parts of a dispersant, and heating the system to the graft polymerization temperature of 30-130° C., to carry out the reaction for 0.5-10 h;
- f. after the end of the reaction, optionally filtering (in the case of using an aqueous phase dispersant), drying to obtain a modified polypropylene;
- g. weighing the modified polypropylene and ungrafted and/or grafted low-modulus polypropylene and optional aids in proportions, mixing and granulating by using a twin-screw extruder at a melting temperature of 180-230° C. and a screw speed of 30-600 rpm, to obtain the modified flexible polypropylene insulating material;
- wherein, the preparation method of the grafted low-modulus polypropylene comprises the following steps:
- i. placing a low-modulus polypropylene in a closed reactor, followed by inert gas replacement;
- ii. mixing an organic solvent and a free radical initiator, and adding the mixture to the closed reactor;
- iii. removing the organic solvent;
- iv. adding a second unsaturated bond-containing polymerizable monomer, adding an interfacial agent, preferably 0-30 parts, and optionally swelling the reaction system, preferably at 20-60° C. for 0-24 h;
- v. optionally adding a dispersant, preferably 0-300 parts, heating the system to the graft polymerization temperature, preferably 30-130° C., to carry out the reaction, preferably for 0.5-10 h;
- vi. after the end of the reaction, optionally filtering (in the case of using an aqueous phase dispersant), drying to obtain a modified low-modulus polypropylene.

According to the method of the invention, if volatile components are present in the system after the end of the reaction, the method of the invention preferably comprises a step of devolatilization, which can be carried out by any conventional method, including vacuum extraction or the use of a stripping agent at the end of the grafting reaction. Suitable stripping agent includes, but is not limited to, an inert gas.

As described above, the term “modified polypropylene” or “modified low-modulus polypropylene” in the invention includes not only a product (crude product) obtained directly by grafting reaction of polypropylene/low-modulus polypropylene and an unsaturated bond-containing polymerizable monomer, but also a graft-modified polypropylene pure product obtained by further purifying the product. Therefore, the preparation method of the invention optionally comprises a step of purifying the crude product. The purification can be carried out by various methods which are conventional in the art, such as extraction.

The invention has no particular limitation on the grafting efficiency of the grafting reaction, but a higher grafting efficiency is more advantageous for obtaining a polypropylene material graft-modified with an unsaturated bond-containing polymerizable monomer having desired properties by a one-step grafting reaction. Therefore, the grafting efficiency of the grafting reaction is preferably controlled to be 20-100%, and more preferably 25-80%. The term “grafting efficiency” is well known to those of ordinary skill in the art, and refers to the amount of unsaturated bond-containing polymerizable monomer on the graft per total amount of unsaturated bond-containing polymerizable monomer charged to the reaction.

The inert gas of the invention may be various inert gases commonly used in the art, including but not limited to nitrogen, argon.

In the method of the invention, the manner of mixing the graft-modified polypropylene with the low-modulus polypropylene and optional additives may be mechanical mixing, preferably twin-screw mechanical blending. The additive is, e.g., any one or more selected from antioxidants, stabilizers, processing aids. The types and amounts of additives used are conventional and known to those of ordinary skill in the art.

The above modified flexible polypropylene insulating material of the invention can be applied to the field of cables, for example, as an insulating material.

The invention will be further described with reference to the following examples, but the scope of the invention is not limited to these examples.

Test Methods
1. Determination of the Comonomer Content in the Polypropylene:

The comonomer content was determined by Spectrum Two type quantitative Fourier Transform Infrared (FTIR) spectroscopy from Perkinelmer company. The correlation of the determined comonomer content was calibrated by quantitative Nuclear Magnetic Resonance (NMR) spectroscopy. The calibration method based on the results obtained from quantitative 1³C-NMR spectroscopy was carried out according to a conventional method in the art.

2. Determination of the Content of Xylene Solubles (XS):

The test was carried out according to the method specified in GB/T24282-2009.

3. Determination of the Comonomer Content in the Xylene Solubles in the Low-Modulus Polypropylene (XSC2) and the Intrinsic Viscosity Ratio of the Xylene Solubles to the Low-Modulus Polypropylene:

The test was carried out using a CRYST-EX instrument from Polymer Char company according to the following steps: dissolving with trichlorobenzene solvent by heating to 150° C., keeping the temperature for 90 min, sampling and testing, then cooling to 35° C., keeping the temperature for 70 min, sampling and testing.

4. Determination of the Weight Average Molecular Weight (M_w) of the Polypropylene:

The sample was dissolved in 1,2,4-trichlorobenzene at a concentration of 1.0 mg/ml and determined by high temperature GPC using PL-GPC 220 type gel permeation chromatograph from Polymer Laboratory company. The test temperature was 150° C. and the solution flow rate was 1.0 ml/min. A standard curve was plotted by taking the molecular weight of polystyrene as an internal reference, and the molecular weight and molecular weight distribution of the sample were calculated according to the outflow time.

5. Determination of the Melt Flow Rate MFR:

The test was carried out at 230° C. under a load of 2.16 kg using 7026 type melt index apparatus from CEAST, according to the method specified in GB/T3682-2018.

6. Determination of the Melting Temperature Tm:

The melting and crystallization processes of the material were analyzed by DSC25 type differential scanning calorimetry from TA company, USA. The specific operation was as follows: under the protection of nitrogen, 5-10 mg of a sample was measured by a three-stage temperature rise and fall measurement method from 20° C. to 200° C., the melting and crystallization processes of the material were reflected by the change of heat flow, and the melting temperature Tm was determined during the secondary heating process.

7. Determination of the Grafting Efficiency GE, the Parameters M1, M2:

2-4 g of the grafted product or crushed composite material particle was put into a Soxhlet extractor, and extracted with an organic solvent (ethyl acetate for aromatic olefin monomers, acrylate monomers and anhydride; acetone for silane monomers) for 24 hours, unreacted monomers and homopolymers were removed, and a pure grafted product was obtained, which was dried and weighed. Then, the parameters Mn, M1, M2 and the grafting efficiency GE were calculated.

(1) The Unsaturated Bond-Containing Polymerizable Monomer is an Alkenyl-Containing Functional Monomer

Parameter Mn (n=A or B) represents the content of the structural units derived from the alkenyl-containing polymerizable monomer and in a grafted state in the component A or component B, and parameter M1 represents the content of the structural units derived from the alkenyl-containing polymerizable monomer and in a grafted state in the composite material, which are calculated from M_Aand M_B. The calculation formulas of M1 and Mn in the invention are as follows:

$Mn = \frac{w_{2} - w_{0}}{w_{1}} \times 100 %$

$M 1 = \frac{M_{A} \times m_{A} + M_{B} \times m_{B}}{m_{product}} \times 100 %$

$GE = \frac{w_{2} - w_{0}}{w_{3}} \times 100 %$

(2) The Unsaturated Bond-Containing Polymerizable Monomer is an Anhydride Monomer and an Alkenyl-Containing Polymerizable Monomer

Parameter Mn (n=A or B) represents the content of the structural units derived from the anhydride monomer and the alkenyl-containing polymerizable monomer and in a grafted state in the component A or component B, and parameter M1 represents the content of the structural units derived from the anhydride monomer and the alkenyl-containing polymerizable monomer and in a grafted state in the composite material, which are calculated from M_Aand M_B. Parameter M2 represents the content of the structural units derived from the anhydride monomer and in a grafted state in the composite material. The calculation formulas of M1, M2 and Mn in the invention are as follows:

$Mn = \frac{w_{2} - w_{0}}{w_{1}} \times 100 %$

$M 1 = \frac{M_{A} \times m_{A} + M_{B} \times m_{B}}{m_{product}} \times 100 %$

$M 2 = \frac{w_{4} \times % G_{NAH}}{m_{product}} \times 100 %$

$GE = \frac{w_{2} - w_{0}}{w_{3}} \times 100 %$

In the above formulas, w₀denotes the mass of the PP matrix; w₁denotes the mass of the grafted product before extraction; w₂denotes the mass of the grafted product after extraction; w₃denotes the total mass of the grafting monomers added; w₄denotes the mass of the composite material after extraction. m_Adenotes the mass of the component A in the composite material, m_Bdenotes the mass of the component B in the composite material, m_productdenotes the mass of the composite material, % G_MAHdenotes the mass content of maleic anhydride. The mass content % G_MAHof maleic anhydride in the composite material was determined and calculated according to the method described in the reference document (Zhang Guangping, Solid Phase Graft of Maleic Anhydride onto Polypropylene in Helical Ribbon Reactor, China Plastics, Vol. 16, No. 2, February, 2002, 69-71).

8. Determination of the Direct Current Volume Resistivity:

The sample to be tested was hot pressed into a sample sheet of 100±10 micron at 210° C. using a vulcanizing press, placed in an oven, and subjected to short-circuit treatment at 80° C. for 6 h to remove residual interference charge on the surface and inside of the sample sheet. Before the test, the sample sheet was wiped with alcohol to remove surface impurities. The test of the sample sheet was carried out according to the method specified in GB/T1410-2006. The testing surface of the sample sheet was subjected to metal spraying treatment. An upper electrode with a diameter of 1 cm and a lower electrode with a diameter of 4 cm were used. The output voltage was 10 kV, the sampling time was 600 s, and the sampling step length was 15 kV/mm. Each sample was determined at 3 points and averaged.

9. Determination of the Breakdown Field Strength:

The sample to be tested was hot pressed into a sample sheet of 100±10 micron at 210° C. using a vulcanizing press, placed in an oven, and subjected to short-circuit treatment at 80° C. for 6 h to remove residual interference charge on the surface and inside of the sample sheet. Before the test, the sample sheet was wiped with alcohol to remove surface impurities. The test of the sample sheet was carried out according to the method specified in GB/T1408-2006. The voltage-rising speed was 1 kV/s, and the breakdown field strength at 20 points was determined for each sample. Then, two-parameter Weibull distribution was used to process the experimental data, to obtain the characteristic breakdown field strength.

10. Determination of the Tensile Strength:

The sample to be tested was injected into a sample bar at 200-220° C., wherein the injection rate was 55 mm/s, the cooling time of the sample in the injection mold was 10 s, and the sample was drawn into a dumbbell-shaped sample bar of 150 mm×10 mm×4 mm. After injection molding, the sample bar needed to be placed aside for 24 h. Then, the test was carried out according to the method specified in GB/T1040.2-2006. The drawing speed of the sample was selected to be 50 mm/min.

11. Determination of the Flexural Modulus:

12. Determination of the Elongation at Break:

The test was carried out according to the method specified in GB/T1040-2006. The sample preparation and test conditions are the same as those for the determination of the tensile strength.

13. Determination of the Dielectric Constant:

The test was carried out according to the method specified in GB/T1409-2006.

14. Characterization of the Rubber Phase:

1 to 2 composite material sample strips with a length of 5-10 cm were taken during twin-screw extrusion and granulation. The composite material sample strips were soaked in liquid nitrogen for 15 min, and then subjected to brittle fracture. The fracture surface of the sample strips was soaked in xylene at room temperature for 24 h, then soaked in clear water with ultrasound for 15 min, finally washed with alcohol, and dried in air. The fracture surface of the sample strips was subjected to metal spraying treatment, and then characterized by a thermal field emission scanning electron microscope (NanoSEM 450 from FEI company, USA).

15. Characterization of Grafted Phase and Calculation of D50

The composite material sample strips were soaked in liquid nitrogen for 15 min and then subjected to brittle fracture. The fracture surface was subjected to metal spraying treatment, and then characterized by a thermal field emission scanning electron microscope (NanoSEM 450 from FEI company, USA), to obtain a micro-morphology picture. Through analysis software, 200 dispersed phases were taken for each sample and the diameter was measured, and D50 was calculated using data processing software. D50 represents the median particle size, that is, the particle size corresponding to the cumulative particle size distribution percentage of a sample reaching 50%.

16. Characterization of Three-Phase Structure

The composite material sample strips were cooled to −50° C. in liquid nitrogen and sliced. The micro-morphology of the composite material was characterized by Dimension type fast scanning atomic force microscope from Bruker company, Germany.

17. Determination of the Content Ratio K of Grafted Units in the Xylene Insolubles and the Modified Flexible Polypropylene Insulating Material

A proper amount of the sample was taken, and accurately weighed, expressed as m_p. Xylene insolubles (IXS) and xylene solubles (XS) were separated, dried and weighed, expressed as m_iXsand m_Xsrespectively, according to the national standard method <<Plastics-Determination of Content of Xylene-Soluble matter in polypropylene>> specified in GB/T24282-2009.

The mass concentration of the grafted units in the xylene insolubles and the modified flexible polypropylene insulating material was measured and calculated by infrared spectroscopy according to the method described in the reference document (Wang Zhengxi, Sun Daotong, Cao Liqun, Application of the Standard Addition Method to Quantitative Infrared Analysis of Polymer [J], Plastic Industry, 1989, (6): 41-43). The references should be chosen to be polymers of grafting monomers, and part of sample references of grafting monomers and the infrared characteristic peaks thereof are exemplified as follows:

Infrared characteristic

Reference
peak

styrene
polystyrene, Shanghai
A700

Secco GPPS-123

methyl methacrylate
poly methyl
A1730

methacrylate, Arkema,

V825

vinyltriethoxysilane
polyvinyltriethoxysilane,
A1082

self made in laboratory

If the grafting monomer includes maleic anhydride, the concentration of maleic anhydride in the xylene insolubles and the modified flexible polypropylene insulating material was determined and calculated according to the method described in the reference document (Zhang Guangping, Solid Phase Graft of Maleic Anhydride onto Polypropylene in Helical Ribbon Reactor, China Plastics, Vol. 16, No. 2, February, 2002, 69-71).

The concentrations of the grafted units in the xylene insolubles and the modified flexible polypropylene insulating material measured and calculated by infrared spectroscopy were expressed as c_{ixs (1, 2, 3 . . . )}and c_{p (1, 2, 3 . . . )}(1, 2, 3 denote different types of grafted units) respectively, and the calculation formula of the mass ratio K of the grafted units in the xylene insolubles and the modified flexible polypropylene insulating material is as follows:

$K = \frac{m_{INS} \times (C_{INS, 1} + C_{INS, 2} + C_{INS, 3} \dots)}{m_{p} \times (C_{p, 1} + C_{p, 2} + C_{p, 3} \dots)}$

EXAMPLES

Raw materials used in the examples and physical properties thereof are listed in Table A, Table B and Table C below.

TABLE A

Name
Description

PP 1*
Self made with a reference to the method

described in CN110305400A

PP 2*
Self made with a reference to the method

described in CN102453180A

PP 3*
Self made with a reference to the method

described in CN102816269A

b-PP 1*
Self made with a reference to the method

described in CN101679557A

b-PP 2*
Self made with a reference to the method

described in CN109153831A

b-PP 3*
Self made with a reference to the method

described in CN101679557A

Dibenzoyl peroxide
J&K Chemicals

Lauroyl peroxide
J&K Chemicals

Tert-butyl peroxy
adamas-beta

(2-ethylhexanoate)

Styrene
J&K Chemicals

Vinyltriethoxysilane
J&K Chemicals

Methyl methacrylate
J&K Chemicals

Polystyrene GPPS-123
Shanghai Secco Petrochemical Co., Ltd.

Maleic anhydride
Sinopharm Chemical Reagent Co., Ltd

Styrene/maleic anhydride
Sigma-Aldrich LLC

copolymer

*PP 1: Homo-polypropylene used in Examples 1A, 4A, 6A, 7A, Comparative Examples 1A, 5A, Examples 1B, 3B, 5B, Comparative Examples 1B, 5B.

*PP 2: Co-polypropylene used in Examples 2A, 3A, 8A, Comparative Examples 3, 4A, Examples 2B, 6B, 7B, Comparative Example 4B.

*PP 3: Co-polypropylene used in Example 5A, Example 4B.

*b-PP 1: Low-modulus polypropylene used in Examples 1A, 2A, 4A, 6A, 7A, 8A, Comparative Examples 3, 4A, 5A, Examples 1B, 3B, 5B, 7B, Comparative Examples 4B, 5B.

*b-PP 2: Low-modulus polypropylene used in Example 3A, Examples 2B, 6B.

*b-PP 3: Low-modulus polypropylene used in Example 5A, Example 4B.

TABLE B

Comonomer
Flexural

MFR.

Mw,
XS,
Type of
content,
modulus,

g/10 min
Tm, ° C.
g/mol
wt %
comonomer
mol %
MPa

PP1
3.4
163.9
38.7E4
0.7
None
0
1630

PP2
3.9
144.3
35.9E4
2.2
1-butene
5.28
1030

PP3
2.5
145.6
36.7E4
6.2
ethylene
3.26
980

TABLE C

Comonomer

Intrinsic
Flexural

MFR.

content,
Mw,
XS,
XSC2,
viscosity
modulus,

g/10 min
Tm, ° C.
wt %
g/mol
wt %
wt %
ratio
MPa

b-PP1
1.2
143.4
18.1
34.3E4
46.8
31.9
0.89
190

b-PP2
0.5
142.5
20.1
53.8E4
65.2
29.5
1.23
90

b-PP3
1.0
133.6
20.3
36.6E4
51.2
29.8
0.58
160

Example 1A

2.0 kg of PP1 powder material was weighed, with fine powder smaller than 40 meshes being removed by sieving, and added to a 10 L reaction kettle with a mechanical stirrer, the reaction system was sealed, and oxygen was removed by nitrogen replacement. 4.83 g tert-butyl peroxy (2-ethylhexanoate) and 322 g styrene were added, the reaction mixture was mixed with stirring for 30 min, 2 kg of a dispersant water was added, swelled at 50° C. for 2 h, the reaction system was heated to 90° C., and reacted for 4 h. After the end of the reaction, the reaction product was cooled, filtered to remove the dispersant water, and dried under vacuum at 70° C. for 10 h, to obtain polypropylene-g-styrene powder, M_A=7.2%.

1.2 kg of polypropylene-g-styrene powder and b-PP1 were weighed according to the mass ratio of 36:64, 3000 ppm antioxidant 1010/168 (mass ratio of 1:1) was added, and the resulting mixture was added into a high-speed stirrer for homogenizing. Granulation was carried out by a twin-screw extruder at the partition temperature of 190-200-210-220-220-220-220-220-210-200° C. and the screw speed of 400 rpm, to obtain the composite material C1A. The product obtained was tested for various performance parameters, and the results are shown in Table 1.

FIG. 1 is an atomic force microscope photograph (modulus image) of the material product of Example 1A in which the bright white regions represent the styrene grafted phase, the black regions represent the rubber phase, and other regions represent the continuous phase.

FIG. 2 is a photograph showing the microstructure of the material product of Example 1A under an electron microscope at 10000 times, in which the spherical dispersed phase is the styrene grafted phase. It can be seen that the particle size of the styrene grafted phase is small and the morphology is regular.

Example 2A

2.0 kg of PP2 powder material was weighed, with fine powder smaller than 40 meshes being removed by sieving, and added to a 10 L reaction kettle with a mechanical stirrer, the reaction system was sealed, and oxygen was removed by nitrogen replacement. 2.4 g dibenzoyl peroxide and 240 g styrene were added, the reaction mixture was mixed with stirring for 30 min, swelled at 40° C. for 2 h, heated to 100° C., and reacted for 3 h. After the end of the reaction, the reaction product was cooled, and dried under vacuum at 70° C. for 10 h, to obtain polypropylene-g-styrene powder, M_A=7.0%.

1.2 kg of polypropylene-g-styrene powder and b-PP1 were weighed according to the mass ratio of 60:40, 3000 ppm antioxidant 1035 was added, and the resulting mixture was added into a high-speed stirrer for homogenizing. Granulation was carried out by a twin-screw extruder at the partition temperature of 190-200-210-220-220-220-220-220-210-200° C. and the screw speed of 450 rpm, to obtain the composite material C2A. The product obtained was tested for various performance parameters, and the results are shown in Table 1.

Example 3A

2.0 kg of PP2 powder material was weighed, with fine powder smaller than 40 meshes being removed by sieving, and added to a 10 L reaction kettle with a mechanical stirrer, the reaction system was sealed, and oxygen was removed by nitrogen replacement. 2.2 g dibenzoyl peroxide and 100 g methyl methacrylate were added, the reaction mixture was mixed with stirring for 20 min, heated to 95° C., and reacted for 5 h. After the end of the reaction, the reaction product was cooled, and dried under vacuum at 70° C. for 10 h, to obtain polypropylene-g-methyl methacrylate powder, M_A=2.5%.

1.2 kg of polypropylene-g-methyl methacrylate powder and b-PP2 were weighed according to the mass ratio of 60:40, 3000 ppm antioxidant 1035 was added, and the resulting mixture was added into a high-speed stirrer for homogenizing. Granulation was carried out by a twin-screw extruder at the partition temperature of 200-210-220-230-230-230-230-220-220-210° C. and the screw speed of 350 rpm, to obtain the composite material C3A. The product obtained was tested for various performance parameters, and the results are shown in Table 1.

FIG. 3 is a photograph showing the microstructure of the material product of Example 3A under an electron microscope at 10000 times, in which the spherical dispersed phase is the methyl methacrylate grafted phase. It can be seen that the particle size of the methyl methacrylate grafted phase is small and the morphology is regular.

Example 4A

2.0 kg of PP1 powder material was weighed, with fine powder smaller than 40 meshes being removed by sieving, and added to a 10 L reaction kettle with a mechanical stirrer, the reaction system was sealed, and oxygen was removed by nitrogen replacement. 3.4 g dibenzoyl peroxide and 226 g styrene were added, the reaction mixture was mixed with stirring for 30 min, 2 L of a dispersant deionized water was added, the reaction system was heated to 90° C., and reacted for 6 h. After the end of the reaction, the reaction product was cooled, and dried under vacuum at 70° C. for 10 h, to obtain polypropylene-g-styrene powder 1, M_A=6.2%.

2.0 kg of b-PP1 powder was weighed, and added to a 10 L reaction kettle with a mechanical stirrer, the reaction system was sealed, and oxygen was removed by nitrogen replacement. 0.28 g dibenzoyl peroxide and 28.0 g styrene were added, the reaction mixture was mixed with stirring for 20 min, 2 L of a dispersant deionized water was added, the reaction system was heated to 90° C., and reacted for 5 h. After the end of the reaction, the reaction product was cooled, and dried under vacuum at 70° C. for 10 h, to obtain polypropylene-g-styrene powder 2, M_B=0.8%.

1.2 kg of polypropylene-g-styrene powder 1 and polypropylene-g-styrene powder 2 were weighed according to the mass ratio of 36:64, 3000 ppm antioxidant 1010/168 (mass ratio of 1:1) was added, and the resulting mixture was added into a high-speed stirrer for homogenizing. Granulation was carried out by a twin-screw extruder at the partition temperature of 190-200-210-220-220-220-220-220-210-200° C. and the screw speed of 400 rpm, to obtain the composite material C4A. The product obtained was tested for various performance parameters, and the results are shown in Table 1.

FIG. 4 is a photograph showing the microstructure of the material product of Example 4A under an electron microscope at 10000 times, in which the spherical dispersed phase is the styrene grafted phase. It can be seen that the particle size of the styrene grafted phase is small and the morphology is regular.

Example 5A

2.0 kg of PP3 powder material was weighed, with fine powder smaller than 40 meshes being removed by sieving, and added to a 10 L reaction kettle with a mechanical stirrer, the reaction system was sealed, and oxygen was removed by nitrogen replacement. 7.5 g of lauroyl peroxide, 150 g of vinyltriethoxysilane and 100 ml of xylene were mixed to homogeneity, added to the reaction kettle, the reaction mixture was mixed with stirring for 20 min, heated to 105° C., and reacted for 4 h. After the end of the reaction, the reaction product was cooled, and dried under vacuum at 70° C. for 10 h, to obtain polypropylene-g-vinyltriethoxysilane powder, M_A=1.8%.

1.2 kg of polypropylene-g-vinyltriethoxysilane powder and b-PP3 were weighed according to the mass ratio of 40:60, 2000 ppm antioxidant 1024 was added, and the resulting mixture was added into a high-speed stirrer for homogenizing. Granulation was carried out by a twin-screw extruder at the partition temperature of 200-210-220-230-230-230-230-220-220-210° C. and the screw speed of 400 rpm, to obtain the composite material C5A. The product obtained was tested for various performance parameters, and the results are shown in Table 1.

FIG. 5 is a photograph showing the microstructure of the material product of Example 5A under an electron microscope at 10000 times, in which the spherical dispersed phase is the vinyltriethoxysilane grafted phase. It can be seen that the particle size of the vinyltriethoxysilane grafted phase is small and the morphology is regular.

Example 6A

2.0 kg of PP1 powder material was weighed, with fine powder smaller than 40 meshes being removed by sieving, and added to a 10 L reaction kettle with a mechanical stirrer, the reaction system was sealed, and oxygen was removed by nitrogen replacement. 4.83 g tert-butyl peroxy (2-ethylhexanoate) and 322 g styrene were added, without stirring, 2 kg of a dispersant water was added, without swelling, the reaction system was heated to 90° C., and reacted for 4 h. After the end of the reaction, the reaction product was cooled, filtered to remove the dispersant water, and dried under vacuum at 70° C. for 10 h, to obtain polypropylene-g-styrene powder, M_A=3.4%.

1.2 kg of polypropylene-g-styrene powder and b-PP1 were weighed according to the mass ratio of 36:64, 3000 ppm antioxidant 1010/168 (mass ratio of 1:1) was added, and the resulting mixture was added into a high-speed stirrer for homogenizing. Granulation was carried out by a twin-screw extruder at the partition temperature of 190-200-210-220-220-220-220-220-210-200° C. and the screw speed of 400 rpm, to obtain the composite material C6A. The product obtained was tested for various performance parameters, and the results are shown in Table 1.

Example 7A

2.0 kg of PP1 powder material was weighed, with fine powder smaller than 40 meshes being removed by sieving, and added to a 10 L reaction kettle with a mechanical stirrer, the reaction system was sealed, and oxygen was removed by nitrogen replacement. 0.9 g dibenzoyl peroxide and 30 g styrene were added, the reaction mixture was mixed with stirring for 30 min, 2 L of a dispersant deionized water was added, the reaction system was heated to 90° C., and reacted for 6 h. After the end of the reaction, the reaction product was cooled, and dried under vacuum at 70° C. for 10 h, to obtain polypropylene-g-styrene powder 1, M_A=0.6%.

2.0 kg of b-PP1 powder was weighed, and added to a 10 L reaction kettle with a mechanical stirrer, the reaction system was sealed, and oxygen was removed by nitrogen replacement. 3.5 g dibenzoyl peroxide and 141 g styrene were added, the reaction mixture was mixed with stirring for 20 min, 2 L of a dispersant deionized water was added, the reaction system was heated to 90° C., and reacted for 5 h. After the end of the reaction, the reaction product was cooled, and dried under vacuum at 70° C. for 10 h, to obtain polypropylene-g-styrene powder 2, M_B=4.1%.

1.2 kg of polypropylene-g-styrene powder 1 and polypropylene-g-styrene powder 2 were weighed according to the mass ratio of 36:64, 3000 ppm antioxidant 1010/168 (mass ratio of 1:1) was added, and the resulting mixture was added into a high-speed stirrer for homogenizing. Granulation was carried out by a twin-screw extruder at the partition temperature of 190-200-210-220-220-220-220-220-210-200° C. and the screw speed of 400 rpm, to obtain the composite material C7A. The product obtained was tested for various performance parameters, and the results are shown in Table 1.

Example 8A

2.0 kg of PP2 powder material was weighed, with fine powder smaller than 40 meshes being removed by sieving, and added to a 10 L reaction kettle with a mechanical stirrer, the reaction system was sealed, and oxygen was removed by nitrogen replacement. 3.1 g dibenzoyl peroxide and 174 g styrene were added, the reaction mixture was mixed with stirring for 30 min, 2 L deionized water was added, swelled at 40° C. for 2 h, the reaction system was heated to 90° C., and reacted for 6 h. After the end of the reaction, the reaction product was cooled, and dried under vacuum at 70° C. for 10 h, to obtain polypropylene-g-styrene powder, M_A=3.6%.

1.2 kg of polypropylene-g-styrene powder and b-PP1 were weighed according to the mass ratio of 50:50, 3000 ppm antioxidant 1035 was added, and the resulting mixture was added into a high-speed stirrer for homogenizing. Granulation was carried out by a twin-screw extruder at the partition temperature of 190-200-210-220-220-220-220-220-210-200° C. and the screw speed of 450 rpm, to obtain the composite material C8A. The product obtained was tested for various performance parameters, and the results are shown in Table 1.

Comparative Example 1A

2.0 kg of PP1 powder material was weighed, with fine powder smaller than 40 meshes being removed by sieving, and added to a 10 L reaction kettle with a mechanical stirrer, the reaction system was sealed, and oxygen was removed by nitrogen replacement. 2 g of dibenzoyl peroxide and 100 g of styrene were added, the reaction mixture was mixed with stirring for 60 min, swelled at 40° C. for 4 h, the reaction system was heated to 95° C., and reacted for 4 h. After the end of the reaction, the reaction product was cooled by nitrogen purging, to obtain polypropylene-g-styrene powder.

1.2 kg of polypropylene-g-styrene powder was weighed, 3000 ppm antioxidant 1010/168 (mass ratio of 1:1) was added, and the resulting mixture was added into a high-speed stirrer for homogenizing. Granulation was carried out by a twin-screw extruder at the partition temperature of 190-200-210-220-220-220-220-220-210-200° C. and the screw speed of 400 rpm, to obtain the product D1A. The product obtained was tested for various performance parameters, and the results are shown in Table 1.

Comparative Example 2

A polypropylene powder with the following characteristics was selected: the comonomer ethylene content is 20.2 mol %, the content of xylene solubles is 44.2 wt %, the weight average molecular weight is 35.3×10⁴g/mol, the MFR under the load of 2.16 kg at 230° C. is 1.55 g/10 min, Tm=143.6° C. 1.2 kg of the above polypropylene powder was weighed, 3000 ppm antioxidant 1010/168 (mass ratio of 1:1) was added, and the resulting mixture was added into a high-speed stirrer for homogenizing. Granulation was carried out by a twin-screw extruder at the partition temperature of 190-200-210-220-220-220-220-220-210-200° C. and the screw speed of 400 rpm, to obtain the product D2. The product obtained was tested for various performance parameters, and the results are shown in Table 1.

Comparative Example 3

1.2 kg of PP2 powder and b-PP1 were weighed according to the mass ratio of 50:50, 3000 ppm antioxidant 1035 was added, and the resulting mixture was added into a high-speed stirrer for homogenizing. Granulation was carried out by a twin-screw extruder at the partition temperature of 190-200-210-220-220-220-220-220-210-200° C. and the screw speed of 450 rpm, to obtain the composite material D3. The product obtained was tested for various performance parameters, and the results are shown in Table 1.

FIG. 6 is a photograph showing the microstructure of the product of Comparative Example 3 under an electron microscope at 10000 times. FIG. 7 is a photograph showing the microstructure of the product of Comparative Example 3 after etching under an electron microscope at 10000 times, wherein the black portions are the rubber phase. It can be seen from FIG. 6 and FIG. 7 that the ungrafted product includes the rubber phase, but does not contain the grafted phase. The product of the invention after grafting is a three-phase structure including both the rubber phase and the grafted phase.

Comparative Example 4A

2.0 kg of PP2 powder material was weighed, with fine powder smaller than 40 meshes being removed by sieving, and added to a 10 L reaction kettle with a mechanical stirrer, the reaction system was sealed, and oxygen was removed by nitrogen replacement. 10 g dibenzoyl peroxide and 566.7 g styrene were added, the reaction mixture was mixed with stirring for 30 min, 2 L deionized water was added, swelled at 40° C. for 2 h, the reaction system was heated to 90° C., and reacted for 6 h. After the end of the reaction, the reaction product was cooled, and dried under vacuum at 70° C. for 10 h, to obtain polypropylene-g-styrene powder, M_A=12.7%.

1.2 kg of polypropylene-g-styrene powder and b-PP1 were weighed according to the mass ratio of 50:50, 3000 ppm antioxidant 1035 was added, and the resulting mixture was added into a high-speed stirrer for homogenizing. Granulation was carried out by a twin-screw extruder at the partition temperature of 190-200-210-220-220-220-220-220-210-200° C. and the screw speed of 450 rpm, to obtain the composite material D4A. The product obtained was tested for various performance parameters, and the results are shown in Table 1.

FIG. 8 is a photograph showing the microstructure of the product of Comparative Example 4A under an electron microscope at 10000 times.

Comparative Example 5A

1.2 kg of PP1, b-PP1, poly styrene GPPS-123 were weighed according to the mass ratio of 31:64:5, 3000 ppm antioxidant 1010/168 (mass ratio of 1:1) was added, and the resulting mixture was added into a high-speed stirrer for homogenizing. Granulation was carried out by a twin-screw extruder at the partition temperature of 190-200-210-220-220-220-220-220-210-200° C. and the screw speed of 400 rpm, to obtain the composite material D5A. The product obtained was tested for various performance parameters, and the results are shown in Table 1.

FIG. 9 is a photograph showing the microstructure of the product of Comparative Example 5A under an electron microscope at 10000 times. Due to poor compatibility, the size of the dispersed phase is not uniform, and there are obvious large-sized dispersed phases.

TABLE 1

Content of

Breakdown
ρ_vg

xylene

Tensile

Flexural
field strength
(110° C.,
Dielectric

MFR
solubles
M1
D50

strength
Elongation
modulus
E_g(110° C.)
40 kV/mm)
constant (50

g/10 min
wt %
wt %
nm
K value
MPa
at break %
MPa
kV/mm
Ω · m
Hz, 110° C.)

C1A
2.4
32.6
2.6
179
0.52
18.3
>300
450
370
1.9E+13
2.2

C2A
1.9
19.7
4.2
171
0.66
16.0
>300
520
316
4.0E+13
2.3

C3A
3.3
29.1
1.5
107
0.76
14.8
>300
480
322
5.2E+13
2.3

C4A
0.9
33.0
2.7
185
0.50
19.0
>300
440
350
2.9E+13
2.2

C5A
1.4
32.3
0.7
137
0.80
12.4
>300
380
304
1.4E+13
2.2

C6A
2.4
34.2
1.2
234
0.25
18.3
>300
450
298
1.1E+13
2.2

C7A
0.8
36.4
2.8
264
0.16
18.7
>300
450
295
1.3E+13
2.2

C8A
1.8
27.5
1.8
192
0.47
15.9
>300
530
310
3.2E+13
2.3

D1A
2.4
1.2
2.1
133
—
36.8
>300
1770
459
1.1E+13
2.2

D2
1.6
44.2
0.0
0
—
14.8
>300
450
227
7.7E+12
2.3

D3
2.3
25.1
0.0
0
—
15.7
>300
530
284
8.6E+12
2.2

D4A
2.1
27.4
6.4
376
0.63
19.7
>300
650
279
1.0E+13
2.3

D5A
1.4
36.1
0.0
323
—
18.3
>300
490
275
9.3E+12
2.2

By comparing the data of Example 1A and Comparative Example 1A, it can be seen that the use of homo-PP as the base powder results in a polypropylene-g-styrene material product having too high flexural modulus and poor mechanical properties, which cannot meet the processing and use requirements of insulating materials.

By comparing the data of Example 1A and Comparative Example 2, it can be seen that the mechanical properties of the product obtained in the invention are not lower than those of the polypropylene prepared by directly alloying in a kettle, and the electrical properties are more advantageous.

By comparing the data of Example 8A and Comparative Example 3, it can be seen that, as compared with the material without the grafted phase, the mechanical properties of the modified flexible polypropylene insulating material are almost the same, and the breakdown field strength and the direct current volume resistivity are both improved, indicating that the modified flexible polypropylene insulating material of the invention has good electrical properties.

By comparing the data of Example 8A and Comparative Example 4A, it can be seen that, when the grafting amount exceeds the limited range, not only the D50 of the grafted phase is too large, which causes a reduction of the breakdown field strength and the volume resistivity of the modified flexible polypropylene insulating material, affecting the electrical properties of the material, but also the flexural modulus of the modified flexible polypropylene insulating material becomes large, which is not favorable for the practical use requirements.

By comparing the data of Example 1A and Comparative Example 5A, it can be seen that, when blending the polymer of alkenyl-containing functional monomer, the size of the dispersed phase of the alkenyl-containing functional monomer becomes too large, which causes a great reduction of the breakdown field strength and the volume resistivity of the material, greatly affecting the electrical properties of the material.

By comparing the data of Example 1A and Examples 6A, 7A, it can be seen that, either by pre-contacting the reaction mixture, or by adjusting the content of grafted units in different polypropylene components, it is possible to increase the proportion of grafted units in the insolubles, resulting in better electrical properties.

In conclusion, as can be seen from the data in Table 1, the modified flexible polypropylene insulating material obtained in the invention not only has excellent electrical insulating properties, but also has good mechanical properties and processability.

Furthermore, it can be seen from the dielectric constant data that the material of the invention satisfies the necessary conditions for insulation.

Example 1B

2.0 kg of PP1 powder material was weighed, with fine powder smaller than 40 meshes being removed by sieving, and added to a 10 L reaction kettle with a mechanical stirrer, the reaction system was sealed, and oxygen was removed by nitrogen replacement. A mixture of 3.95 g tert-butyl peroxy (2-ethylhexanoate) and 30 g maleic anhydride and 120 g styrene was added, mixed with stirring for 30 min, 2 kg of a dispersant water was added, swelled at 50° C. for 2, the reaction system was heated to 90° C., and reacted for 4 h. After the end of the reaction, the reaction product was cooled, filtered to remove the dispersant water, and dried under vacuum at 70° C. for 10 h, to obtain polypropylene-g-styrene/maleic anhydride powder, M_A=4.9%.

1.2 kg of polypropylene-g-styrene/maleic anhydride powder and b-PP1 were weighed according to the mass ratio of 36:64, 3000 ppm antioxidant 1010/168 (mass ratio of 1:1) was added, and the resulting mixture was added into a high-speed stirrer for homogenizing. Granulation was carried out by a twin-screw extruder at the partition temperature of 190-200-210-220-220-220-220-220-210-200° C. and the screw speed of 400 rpm, to obtain the composite material C₁B. The product obtained was tested for various performance parameters, and the results are shown in Table 1.

FIG. 10 is an atomic force microscope photograph (Log modulus mode) of the material product of Example 1B in which the white regions represent the styrene/maleic anhydride grafted phase, the black regions represent the rubber phase, and other regions represent the continuous phase.

FIG. 11 is a photograph showing the microstructure of the material product of Example 1B under an electron microscope at 20000 times, in which the spherical dispersed phase is the styrene/maleic anhydride grafted phase. It can be seen that the particle size of the styrene/maleic anhydride grafted phase is small and the morphology is regular.

Example 2B

2.0 kg of PP2 powder material was weighed, with fine powder smaller than 40 meshes being removed by sieving, and added to a 10 L reaction kettle with a mechanical stirrer, the reaction system was sealed, and oxygen was removed by nitrogen replacement. A mixture of 1.5 g dibenzoyl peroxide and 13 g maleic anhydride and 39 g styrene was added, mixed with stirring for 30 min, swelled at 40° C. for 2 h, the reaction system was heated to 100° C., and reacted for 3 h. After the end of the reaction, the reaction product was cooled, and dried under vacuum at 70° C. for 10 h, to obtain polypropylene-g-styrene/maleic anhydride powder, M_A=1.4%.

1.2 kg of polypropylene-g-styrene/maleic anhydride powder and b-PP2 were weighed according to the mass ratio of 60:40, 3000 ppm antioxidant 1035 was added, and the resulting mixture was added into a high-speed stirrer for homogenizing. Granulation was carried out by a twin-screw extruder at the partition temperature of 190-200-210-220-220-220-220-220-210-200° C. and the screw speed of 450 rpm, to obtain the composite material C₂B. The product obtained was tested for various performance parameters, and the results are shown in Table 2. FIG. 12 is a photograph showing the microstructure of the material product of Example 2B under an electron microscope at 20000 times, in which the spherical dispersed phase is the styrene/maleic anhydride grafted phase. It can be seen that the particle size of the styrene/maleic anhydride grafted phase is small and the morphology is regular.

Example 3B

2.0 kg of PP1 powder material was weighed, with fine powder smaller than 40 meshes being removed by sieving, and added to a 10 L reaction kettle with a mechanical stirrer, the reaction system was sealed, and oxygen was removed by nitrogen replacement. A mixture of 3.95 g tert-butyl peroxy (2-ethylhexanoate) and 30 g maleic anhydride and 120 g styrene was added, mixed with stirring for 30 min, 2 kg of a dispersant water was added, swelled at 50° C. for 2 h, the reaction system was heated to 90° C., and reacted for 4 h. After the end of the reaction, the reaction product was cooled, filtered to remove the dispersant water, and dried under vacuum at 70° C. for 10 h, to obtain polypropylene-g-styrene/maleic anhydride powder, M_A=4.9%.

2.0 kg of b-PP1 powder was weighed, and added to a 10 L reaction kettle with a mechanical stirrer, the reaction system was sealed, and oxygen was removed by nitrogen replacement. A mixture of 0.28 g dibenzoyl peroxide and 64.0 g styrene was added, mixed with stirring for 20 min, 2 L of a dispersant deionized water was added, the reaction system was heated to 90° C., and reacted for 5 h. After the end of the reaction, the reaction product was cooled, and dried under vacuum at 70° C. for 10 h, to obtain polypropylene-g-styrene powder, M_B=1.1%.

1.2 kg of polypropylene-g-styrene/maleic anhydride powder and polypropylene-g-styrene powder were weighed according to the mass ratio of 38:62, 3000 ppm antioxidant 1010/168 (mass ratio of 1:1) was added, and the resulting mixture was added into a high-speed stirrer for homogenizing. Granulation was carried out by a twin-screw extruder at the partition temperature of 190-200-210-220-220-220-220-220-210-200° C. and the screw speed of 400 rpm, to obtain the composite material C3B. The product obtained was tested for various performance parameters, and the results are shown in Table 2.

FIG. 13 is a photograph showing the microstructure of the material product of Example 3B under an electron microscope at 20000 times, in which the spherical dispersed phase is the styrene/maleic anhydride grafted phase. It can be seen that the particle size of the styrene/maleic anhydride grafted phase is small and the morphology is regular.

Example 4B

2.0 kg of PP3 powder material was weighed, with fine powder smaller than 40 meshes being removed by sieving, and added to a 10 L reaction kettle with a mechanical stirrer, the reaction system was sealed, and oxygen was removed by nitrogen replacement. A mixture of 3.5 g lauroyl peroxide and 30 g maleic anhydride and 32 g α-methylstyrene was mixed with stirring for 30 min, 2 L of a dispersant deionized water was added, the reaction system was heated to 90° C., and reacted for 6 h. After the end of the reaction, the reaction product was cooled, and dried under vacuum at 70° C. for 10 h, to obtain polypropylene-g-α-methylstyrene/maleic anhydride powder, M_A=0.9%.

1.2 kg of polypropylene-g-α-methylstyrene/maleic anhydride powder and b-PP3 were weighed according to the mass ratio of 41:59, 2000 ppm antioxidant 1024 was added, and the resulting mixture was added into a high-speed stirrer for homogenizing. Granulation was carried out by a twin-screw extruder at the partition temperature of 200-210-220-230-230-230-230-220-220-210° C. and the screw speed of 400 rpm, to obtain the composite material C₄B. The product obtained was tested for various performance parameters, and the results are shown in Table 2.

Example 5B

2.0 kg of PP1 powder material was weighed, with fine powder smaller than 40 meshes being removed by sieving, and added to a 10 L reaction kettle with a mechanical stirrer, the reaction system was sealed, and oxygen was removed by nitrogen replacement. A mixture of 1.8 g dibenzoyl peroxide and 120.5 g methyl methacrylate was added, mixed with stirring for 30 min, 2 L of a dispersant deionized water was added, the reaction system was heated to 90° C., and reacted for 2.5 h. After the end of the reaction, the reaction product was cooled, and dried under vacuum at 70° C. for 10 h, to obtain polypropylene-g-methyl methacrylate powder, M_A=4.6%.

2.0 kg of b-PP1 powder was weighed, and added to a 10 L reaction kettle with a mechanical stirrer, the reaction system was sealed, and oxygen was removed by nitrogen replacement. A mixture of 0.29 g dibenzoyl peroxide and 14.3 g maleic anhydride and 85.7 g styrene was added, mixed with stirring for 20 min, the reaction system was heated to 90° C., and reacted for 5 h. After the end of the reaction, the reaction product was cooled, and dried under vacuum at 70° C. for 10 h, to obtain polypropylene-g-styrene/maleic anhydride powder, M_B=2.6%.

1.2 kg of polypropylene-g-methyl methacrylate powder and polypropylene-g-styrene/maleic anhydride powder were weighed according to the mass ratio of 38:62, 3000 ppm antioxidant 1010/168 (mass ratio of 1:1) was added, and the resulting mixture was added into a high-speed stirrer for homogenizing. Granulation was carried out by a twin-screw extruder at the partition temperature of 190-200-210-220-220-220-220-220-210-200° C. and the screw speed of 400 rpm, to obtain the composite material C5B. The product obtained was tested for various performance parameters, and the results are shown in Table 2.

Example 6B

2.0 kg of PP2 powder material was weighed, with fine powder smaller than 40 meshes being removed by sieving, and added to a 10 L reaction kettle with a mechanical stirrer, the reaction system was sealed, and oxygen was removed by nitrogen replacement. A mixture of 1.5 g dibenzoyl peroxide and 13 g maleic anhydride and 39 g styrene was added, mixed with stirring for 30 min, swelled at 40° C. for 2 h, the reaction system was heated to 100° C., and reacted for 3 h. After the end of the reaction, the reaction product was cooled, and dried under vacuum at 70° C. for 10 h, to obtain polypropylene-g-styrene/maleic anhydride powder, M_A=1.4%.

2.0 kg of b-PP2 powder was weighed, and added to a 10 L reaction kettle with a mechanical stirrer, the reaction system was sealed, and oxygen was removed by nitrogen replacement. A mixture of 0.6 g dibenzoyl peroxide and 8.4 g maleic anhydride and 31.5 g styrene was added, mixed with stirring for 20 min, 2 L of a dispersant deionized water was added, the reaction system was heated to 90° C., and reacted for 5 h. After the end of the reaction, the reaction product was cooled, and dried under vacuum at 70° C. for 10 h, to obtain polypropylene-g-styrene/maleic anhydride powder 2, M_B=1.3%.

1.2 kg of polypropylene-g-styrene/maleic anhydride powder 1 and polypropylene-g-styrene/maleic anhydride powder 2 were weighed according to the mass ratio of 60:40, 3000 ppm antioxidant 1035 was added, and the resulting mixture was added into a high-speed stirrer for homogenizing. Granulation was carried out by a twin-screw extruder at the partition temperature of 190-200-210-220-220-220-220-220-210-200° C. and the screw speed of 450 rpm, to obtain the composite material C6B. The product obtained was tested for various performance parameters, and the results are shown in Table 2.

Example 7B

2.0 kg of PP2 powder material was weighed, with fine powder smaller than 40 meshes being removed by sieving, and added to a 10 L reaction kettle with a mechanical stirrer, the reaction system was sealed, and oxygen was removed by nitrogen replacement. A mixture of 1.7 g dibenzoyl peroxide and 17 g maleic anhydride and 68 g styrene was added, mixed with stirring for 30 min, 2 L deionized water was added, swelled at 40° C. for 2 h, the reaction system was heated to 90° C., and reacted for 6 h. After the end of the reaction, the reaction product was cooled, and dried under vacuum at 70° C. for 10 h, to obtain polypropylene-g-styrene/maleic anhydride powder, M_A=2.2 00.

1.2 kg of polypropylene-g-styrene/maleic anhydride powder and b-PP1 were weighed according to the mass ratio of 50:50, 3000 ppm antioxidant 1035 was added, and the resulting mixture was added into a high-speed stirrer for homogenizing. Granulation was carried out by a twin-screw extruder at the partition temperature of 190-200-210-220-220-220-220-220-210-200° C. and the screw speed of 450 rpm, to obtain the composite material C7B. The product obtained was tested for various performance parameters, and the results are shown in Table 2.

Comparative Example 1B

After the end of the reaction, the reaction product was cooled by nitrogen purging, to obtain polypropylene-g-styrene/maleic anhydride powder. 1.2 kg of polypropylene-g-styrene/maleic anhydride powder was weighed, 3000 ppm antioxidant 1010/168 (mass ratio of 1:1) was added, and the resulting mixture was added into a high-speed stirrer for homogenizing. Granulation was carried out by a twin-screw extruder at the partition temperature of 190-200-210-220-220-220-220-220-210-200° C. and the screw speed of 400 rpm, to obtain the product D1B. The product obtained was tested for various performance parameters, and the results are shown in Table 2.

Comparative Example 4B

2.0 kg of PP2 powder material was weighed, with fine powder smaller than 40 meshes being removed by sieving, and added to a 10 L reaction kettle with a mechanical stirrer, the reaction system was sealed, and oxygen was removed by nitrogen replacement. A mixture of 10 g dibenzoyl peroxide and 100 g maleic anhydride and 400 g styrene was added, mixed with stirring for 30 min, 2 L deionized water was added, swelled at 40° C. for 2 h, the reaction system was heated to 90° C., and reacted for 6 h. After the end of the reaction, the reaction product was cooled, and dried under vacuum at 70° C. for 10 h, to obtain polypropylene-g-styrene/maleic anhydride powder, M_A=13.4%.

1.2 kg of polypropylene-g-styrene/maleic anhydride powder and b-PP1 were weighed according to the mass ratio of 50:50, 3000 ppm antioxidant 1035 was added, and the resulting mixture was added into a high-speed stirrer for homogenizing. Granulation was carried out by a twin-screw extruder at the partition temperature of 190-200-210-220-220-220-220-220-210-200° C. and the screw speed of 450 rpm, to obtain the composite material D4B. The product obtained was tested for various performance parameters, and the results are shown in Table 2. FIG. 14 is a photograph showing the microstructure of the product of Comparative Example 4B under an electron microscope at 20000 times.

Comparative Example 5B

1.2 kg of PP1, b-PP1, styrene/maleic anhydride polymer were weighed according to the mass ratio of 31:64:5, 3000 ppm antioxidant 1010/168 (mass ratio of 1:1) was added, and the resulting mixture was added into a high-speed stirrer for homogenizing. Granulation was carried out by a twin-screw extruder at the partition temperature of 190-200-210-220-220-220-220-220-210-200° C. and the screw speed of 400 rpm, to obtain the composite material D5B. The product obtained was tested for various performance parameters, and the results are shown in Table 2.

FIG. 15 is a photograph showing the microstructure of the product of Comparative Example 5B under an electron microscope at 20000 times. Due to poor compatibility, the size of the dispersed phase is not uniform, and there are obvious large-sized dispersed phases.

TABLE 2

Content of

Breakdown
ρ_vg

xylene

Tensile

Flexural
field strength
(110° C.,
Dielectric

MFR
solubles
M1
M2
D50

strength
Elongation
modulus
E_g(110° C.)
40 kV/mm)
constant (50

g/10 min
wt %
wt %
wt %
nm
K value
MPa
at break %
MPa
kV/mm
Ω · m
Hz, 110° C.)

C1B
1.5
32.5
1.8
0.4
104
0.85
18.0
>300
430
327
7.4E+13
2.3

C2B
2.3
27.8
0.8
0.2
66
0.82
15.9
>300
550
322
4.8E+13
2.4

C3B
1.2
31.6
2.5
0.3
99
0.58
18.2
>300
450
310
5.1E+13
2.3

C4B
2.4
43.1
0.4
0.1
50
0.79
12.3
>300
360
297
3.3E+13
2.3

C5B
1.4
33.4
3.4
0.2
119
0.57
18.9
>300
490
289
3.8E+13
2.3

C6B
2.2
29.6
1.4
0.3
85
0.52
16.8
>300
520
324
5.6E+13
2.3

C7B
2.2
25.2
1.1
0.2
84
0.60
15.9
>300
530
304
4.1E+13
2.3

D1B
1.9
1.5
1.4
0.4
45
—
36.1
>300
1570
419
9.2E+13
2.2

D2
1.6
44.2
0.0
0.0
0
—
14.8
>300
450
227
7.7E+12
2.3

D3
2.3
25.1
0.0
0.0
0
—
15.7
>300
530
284
8.6E+12
2.2

D4B
2.4
24.4
6.7
1.3
175
0.75
16.5
>300
540
214
2.1E+14
2.4

D5B
2.2
31.2
0.0
0.0
187
—
17.3
>300
430
210
6.9E+12
2.2

By comparing the data of Example 1B and Comparative Example 1B, it can be seen that the use of homo-PP as the base powder results in a polypropylene-g-styrene/maleic anhydride material product having too high flexural modulus and poor mechanical properties, which cannot meet the processing and use requirements of insulating materials.

By comparing the data of Example 1B and Comparative Example 2, it can be seen that the mechanical properties of the product obtained in the invention are not lower than those of the polypropylene prepared by directly alloying in a kettle, and the electrical properties are more advantageous.

By comparing the data of Example 7B and Comparative Example 3, it can be seen that, as compared with the material without the grafted phase, the mechanical properties of the modified flexible polypropylene insulating material are almost the same, and the breakdown field strength and the direct current volume resistivity are both improved, indicating that the modified flexible polypropylene insulating material of the invention has good electrical properties.

By comparing the data of Example 7B and Comparative Example 4B, it can be seen that, when the amount of the grafting monomer added is too high (M1 value is too high), the D50 of the grafted phase is too large, which causes a great reduction of the breakdown field strength of the modified flexible polypropylene insulating material, failing to meet the practical use requirements.

By comparing the data of Example 1B and Comparative Example 5B, it can be seen that, when blending the copolymer of anhydride/alkenyl-containing functional monomer, the size of the dispersed phase becomes too large and the dispersion is not uniform, which causes a great reduction of the breakdown field strength and the volume resistivity of the material, greatly affecting the electrical properties of the material.

In conclusion, as can be seen from the data in Table 2, the modified flexible polypropylene insulating material obtained in the invention not only has excellent electrical insulating properties, but also has good mechanical properties.

Furthermore, it can be seen from the dielectric constant data that the material of the invention satisfies the necessary conditions for insulation.

The examples of the invention have been described above, the above description is exemplary, not exhaustive, and the invention is not limited to the examples. Without departing from the scope and spirit of the examples, many modifications and changes are obvious to those of ordinary skill in the art.

The endpoints of ranges and any values disclosed herein are not to be limited to the precise ranges or values, which are to be understood to encompass values close to those ranges or values. For numerical ranges, the endpoints of each range, the endpoints of each range and the individual point values, as well as the individual point values may be combined with each other to yield one or more new numerical ranges, which numerical ranges should be deemed to be specifically disclosed herein.

Claims

1. A modified flexible polypropylene insulating material comprising a propylene-based continuous phase, and a rubber phase and a grafted phase derived from an unsaturated bond-containing polymerizable monomer dispersed in the propylene-based continuous phase; wherein, the modified flexible polypropylene insulating material has a content of xylene solubles ranging from 10 wt % to 55 wt %, preferably from 15 wt % to 45 wt %, more preferably from 18 wt % to 40 wt %, and still more preferably from 20 wt % to 40 wt %, based on the total weight of the modified flexible polypropylene insulating material; the content of structural units derived from the unsaturated bond-containing polymerizable monomer and in a grafted state in the modified flexible polypropylene insulating material ranges from 0.3 wt % to 6 wt %, and preferably from 0.7 wt % to 5 wt %; the flexural modulus of the modified flexible polypropylene insulating material ranges from 200 MPa to 1000 MPa, preferably from 200 MPa to 950 MPa, more preferably from 200 MPa to 700 MPa, and still more preferably from 250 MPa to 600 MPa; preferably, the ratio of the mass of the structural units derived from the unsaturated bond-containing polymerizable monomer in xylene insolubles to the mass of the structural units derived from the unsaturated bond-containing polymerizable monomer in the modified flexible polypropylene insulating material is more than 0.1, preferably from 0.3 to 0.9.
2. The modified flexible polypropylene insulating material according to claim 1, wherein the unsaturated bond-containing polymerizable monomer is an alkenyl-containing functional monomer; the content of structural units derived from the alkenyl-containing functional monomer and in a grafted state in the modified flexible polypropylene insulating material ranges from 0.4 wt % to 6 wt %, and preferably from 1 wt % to 5 wt %; the D50 of the grafted phase is less than 300 nm, preferably from 10 nm to 250 nm, and more preferably from 50 nm to 200 nm.
3. The modified flexible polypropylene insulating material according to claim 1, wherein the unsaturated bond-containing polymerizable monomer is an anhydride monomer and an alkenyl-containing functional monomer; the content of structural units derived from the anhydride monomer and the alkenyl-containing functional monomer and in a grafted state in the modified flexible polypropylene insulating material ranges from 0.3 wt % to 5 wt %, preferably from 0.7 wt % to 3 wt, and the content of structural units derived from the anhydride monomer and in a grafted state ranges from 0.05 wt % to 2 wt %, preferably from 0.2 wt % to 0.5 wt %; the D50 of the grafted phase is less than 170 nm, preferably from 10 nm to 150 nm, and more preferably from 55 nm to 110 nm.
4. The modified flexible polypropylene insulating material according to claim 1, wherein the modified flexible polypropylene insulating material has at least one of the following characteristics: the melt flow rate under the load of 2.16 kg at 230° C. ranges from 0.5 g/10 min to 15 g/10 min, preferably from 0.6 g/10 min to 10 g/10 min, and further preferably 0.8 g/10 min to 6 g/10 min; the elongation at break is greater than or equal to 200%, and preferably greater than or equal to 300%; the tensile strength is more than 5 MPa, preferably from 10 MPa to 25 MPa.
5. The modified flexible polypropylene insulating material according to claim 1, wherein the modified flexible polypropylene insulating material has at least one of the following characteristics: the maximum working temperature of the modified flexible polypropylene insulating material is greater than or equal to 90° C., preferably from 100° C. to 160° C., and more preferably from 110° C. to 140° C.;the breakdown field strength E9 at 110° C. of the modified flexible polypropylene insulating material is greater than or equal to 285 kV/mm, preferably from 290 kV/mm to 800 kV/mm, and more preferably from 300 kV/mm to 750 kV/mm;the direct current volume resistivity ρvg at 110° C. and 40 kV/mm field strength of the modified flexible polypropylene insulating material is greater than or equal to 1.0×1013 Ω·m, preferably from 1.5×1013 Ω·m to 1.0×1020 Ω·m;the dielectric constant at 110° C. and 50 Hz of the modified flexible polypropylene insulating material is greater than 2.0, and preferably ranging from 2.1 to 2.5.
6. The modified flexible polypropylene insulating material according to claim 3, wherein the anhydride monomer is selected from anhydrides having at least one olefinic unsaturation; preferably, the anhydride monomer is selected from maleic anhydride and itaconic anhydride; further preferably, the anhydride monomer is maleic anhydride.
7. The modified flexible polypropylene insulating material according to claim 2, wherein the alkenyl-containing functional monomer is selected from at least one of monomers having a structure represented by formula 1,
8. The modified flexible polypropylene insulating material according to claim 7, wherein Rb, Rc, Rd are each independently selected from H and substituted or unsubstituted C1-C6 alkyl; preferably Rb, Rc, Rd are each independently selected from H and substituted or unsubstituted C1-C3 alkyl; Ra is selected from substituted or unsubstituted C1-C20 alkyl, substituted or unsubstituted C1-C20 alkoxy, substituted or unsubstituted C6-C20 aryl, substituted or unsubstituted C1-C20 ester group, substituted or unsubstituted C1-C20 carboxyl, substituted or unsubstituted C3-C20 cycloalkyl, substituted or unsubstituted C3-C20 heterocyclyl, cyano, and substituted or unsubstituted C3-C20 silyl; the substituent group is selected from halogen, hydroxy, amino, C1-C12 alkyl, C3-C6 cycloalkyl, C1-C12 alkoxy, and C1-C12 acyloxy; preferably, Ra is selected from substituted or unsubstituted C1-C12 alkyl, substituted or unsubstituted C1-C18 alkoxy, substituted or unsubstituted C6-C12 aryl, substituted or unsubstituted C1-C12 ester group, substituted or unsubstituted C1-C12 carboxyl, substituted or unsubstituted C3-C12 cycloalkyl or heterocyclyl, and cyano; preferably, the substituent group is selected from halogen, C1-C6 alkyl, and C3-C6 cycloalkyl; more preferably, Ra is selected from substituted or unsubstituted C1-C6 alkyl, substituted or unsubstituted C1-C12 alkoxy, substituted or unsubstituted C6-C8 aryl, substituted or unsubstituted C1-C6 ester group, substituted or unsubstituted C1-C6 carboxyl, substituted or unsubstituted C3-C6 cycloalkyl, substituted or unsubstituted C3-C6 heterocyclyl, and cyano.
9. The modified flexible polypropylene insulating material according to claim 8, wherein Rb, Rc, Rd are each independently selected from H and substituted or unsubstituted C1-C6 alkyl; Ra is selected from a group of formula 2, a group of formula 3, a group of formula 4, a group of formula 5, a group of formula 6, a group that is a combination of a group of formula 6 and a group of formula 7, and a heterocyclic group;
10. The modified flexible polypropylene insulating material according to claim 9, wherein the alkenyl-containing functional monomer is an aromatic olefin monomer, the aromatic olefin monomer is at least one selected from styrene, α-methylstyrene, 1-vinyl naphthalene, 2-vinyl naphthalene, mono- or polysubstituted styrene, mono- or polysubstituted α-methylstyrene, mono- or polysubstituted 1-vinyl naphthalene, and mono- or polysubstituted 2-vinyl naphthalene; further wherein the substituent group preferably is selected from halogen, hydroxy, amino, phosphoric group, sulfonic group, C1-C8 linear alkyl, C3-C8 branched alkyl, C3-C8 cycloalkyl, C1-C6 linear alkoxy, C3-C8 branched alkoxy, C3-C8 cycloalkoxy, C1-C8 linear ester group, C3-C8 branched ester group, C3-C8 cyclic ester group, C1-C8 linear amine group, C3-C8 branched amine group, and C3-C8 cyclic amine group; preferably, the aromatic olefin monomer is at least one selected from styrene, α-methylstyrene, 2-methylstyrene, 3-methylstyrene, and 4-methylstyrene; and/or the alkenyl-containing functional monomer is an alkenyl-containing silane monomer, wherein the alkenyl-containing silane monomer is at least one selected from vinyltriethoxysilane, vinyltrimethoxysilane, vinyltriisopropoxysilane, vinyltri-tert-butoxysilane, vinyltriacetoxysilane, methylvinyldimethoxysilane, ethylvinyldiethoxysilane, allyltriethoxysilane, allyltrimethoxysilane, allyltriisopropoxysilane, vinyltris(β-methoxyethoxy)silane, allyltris(β-methoxyethoxy)silane, allyltri-tert-butoxysilane, allyltriacetoxysilane, methylallyldimethoxysilane, and ethylallyldiethoxysilane; and/orthe alkenyl-containing functional monomer is an acrylate monomer and an optional acrylic monomer, preferably, the acrylate monomer is at least one selected from methyl (methyl)acrylate, sec-butyl (methyl)acrylate, ethyl (methyl)acrylate, n-butyl (methyl)acrylate, isobutyl (methyl)acrylate, tert-butyl (methyl)acrylate, isooctyl (methyl)acrylate, dodecyl (methyl)acrylate, cocinin (methyl)acrylate, octadecyl (methyl)acrylate, dimethylaminoethyl (methyl)acrylate, diethylaminoethyl (methyl)acrylate, dimethylaminopropyl (methyl)acrylate, and glycidyl (methyl)acrylate; preferably, the acrylic monomer is at least one selected from acrylic acid, methacrylic acid and 2-ethylacrylic acid; preferably, the molar ratio of the structural units derived from the acrylate monomer to the structural units derived from the acrylic monomer ranges from 1:0 to 1:2, preferably from 1:0.125 to 1:1.
11. The modified flexible polypropylene insulating material according to claim 10, wherein the alkenyl-containing polymerizable monomer is at least one selected from vinyl acetate, styrene, α-methylstyrene, (meth)acrylate, vinyl alkyl ether, vinyl pyrrolidone, vinyl pyridine, vinyl imidazole, and acrylonitrile; the (meth)acrylate is preferably at least one selected from methyl (meth)acrylate, ethyl (meth)acrylate, and glycidyl (meth)acrylate; preferably, the alkenyl-containing polymerizable monomer is selected from vinyl acetate, styrene, and α-methylstyrene; further preferably, the alkenyl-containing polymerizable monomer is styrene.
12. The modified flexible polypropylene insulating material according to claim 1, wherein the modified flexible polypropylene insulating material comprises modified polypropylene (A) which is polypropylene graft-modified with a first unsaturated bond-containing polymerizable monomer, and low-modulus polypropylene (B) which is unmodified low-modulus polypropylene and/or low-modulus polypropylene graft-modified with a second unsaturated bond-containing polymerizable monomer; preferably, the first unsaturated bond-containing polymerizable monomer and the second unsaturated bond-containing polymerizable monomer are each independently an alkenyl-containing functional monomer and optionally an anhydride monomer;preferably, the content of the modified polypropylene (A) ranges from 20 wt % to 80 wt %, preferably from 30 wt % to 70 wt %, and more preferably from 35 wt % to 65 wt %, and the content of the low-modulus polypropylene (B) ranges from 20 wt % to 80 wt %, preferably from 30 wt % to 70 wt %, and more preferably from 35 wt % to 65 wt %, based on the total weight of the modified flexible polypropylene insulating material.
13. The modified flexible polypropylene insulating material according to claim 12, wherein the modified flexible polypropylene insulating material is prepared by blending the modified polypropylene (A) with the low-modulus polypropylene (B).
14. The modified flexible polypropylene insulating material according to claim 13, wherein the modified polypropylene (A) comprises structural units derived from homo- or co-polypropylene and structural units derived from the unsaturated bond-containing polymerizable monomer; the content of the structural units derived from the unsaturated bond-containing polymerizable monomer and in a grafted state in the modified polypropylene (A) ranges from 0.1 wt % to 20 wt %, preferably from 1 wt % to 15 wt %, based on the weight of the modified polypropylene (A).
15. The modified flexible polypropylene insulating material according to claim 14, wherein the homo- or co-polypropylene has at least one of the following characteristics: the comonomer content ranges from 0 mol % to 15 mol %, preferably from 0 mol % to 12 mol %, more preferably from 0 mol % to 8 mol %; the content of xylene solubles is less than 15 wt %, preferably from 0.5 wt % to 8 wt %; the melt flow rate under a load of 2.16 kg at 230° C. ranges from 1 g/10 min to 10 g/10 min, preferably from 2 g/10 min to 5 g/10 min; the melting temperature Tm ranges from 110° C. to 180° C., further preferably from 120° C. to 170° C.; the weight average molecular weight ranges from 20×104 g/mol to 50×104 g/mol; the flexural modulus ranges from 500 MPa to 2000 MPa, preferably from 600 MPa to 1700 MPa; the elongation at break is greater than or equal to 200%, preferably greater than or equal to 300%, the tensile strength is greater than 5 MPa, preferably from 10 MPa to −40 MPa.
16. The modified flexible polypropylene insulating material according to claim 14, wherein the comonomer of the co-polypropylene is at least one selected from ethylene and C4-C8 α-olefin; preferably, the comonomer of the co-polypropylene is at least one selected from ethylene, 1-butene, 1-pentene, 4-methyl-1-pentene, 1-hexene, 1-heptene, and 1-octene; further preferably, the comonomer of the co-polypropylene is ethylene and/or 1-butene; the comonomer content ranges from 0.1 mol % to 15 mol %, preferably from 0.1 mol % to 12 mol %, and more preferably from 0.1 mol % to 8 mol %, based on the total molar amount of the monomers.
17. The modified flexible polypropylene insulating material according to claim 12, wherein the low-modulus polypropylene is a copolymer of propylene with ethylene or a higher alpha-olefin, having a flexural modulus of less than 300 MPa; preferably the low-modulus polypropylene is an ethylene-propylene copolymer; preferably, the copolymer of propylene with ethylene or a higher alpha-olefin comprises a propylene homopolymer and/or propylene random copolymer matrix component (1) and, dispersed therein, another propylene copolymer component (2);more preferably, the low-modulus polypropylene is of sea-island structure or co-continuous structure;further preferably, the low-modulus polypropylene is prepared in situ in a reactor.
18. The modified flexible polypropylene insulating material according to claim 17, wherein the low-modulus polypropylene has at least one of the following characteristics: the comonomer content ranges from 8 wt % to 25 wt %, preferably from 10 wt % to 22 wt %; the content of xylene solubles ranges from 18 wt % to 75 wt %, preferably from 30 wt % to 70 wt %, and more preferably from 30 wt % to 67 wt %; the melt flow rate under a load of 2.16 kg at 230° C. ranges from 0.1 g/10 min to 15 g/10 min, preferably from 0.2 q/10 min to 7 g/10 min; the melting temperature Tm ranges from 120° C. to 165° C., and further preferably from 125° C. to 150° C.; the flexural modulus ranges from 10 MPa to 300 MPa, preferably from 15 MPa to 250 MPa; the comonomer content in the xylene solubles ranges from 10 wt % to 50 wt %, preferably from 20 wt % to 35 wt %; the intrinsic viscosity ratio of the xylene solubles to the low-modulus polypropylene ranges from 0.5 to 3, preferably from 0.8 to 1.3; the weight average molecular weight ranges from 25×104 g/mol to 70×104 g/mol.
19. The modified flexible polypropylene insulating material according to claim 12, wherein the content of the structural units in a grafted state in the low-modulus polypropylene (B) ranges from 0 wt % to 5 wt %, preferably from 0.2 wt % to 2.5 wt %, based on the weight of the low-modulus polypropylene (B).
20. A method for preparing the modified flexible polypropylene insulating material according to claim 1, comprising: blending modified polypropylene (A) and low-modulus polypropylene (B) to prepare the modified flexible polypropylene insulating material, wherein modified polypropylene (A) is polypropylene graft-modified with a first unsaturated bond-containing polymerizable monomer, and the low-modulus polypropylene (B) is unmodified low-modulus polypropylene and/or low-modulus polypropylene graft-modified with a second unsaturated bond-containing polymerizable monomer; preferably, the first unsaturated bond-containing polymerizable monomer and the second unsaturated bond-containing polymerizable monomer are each independently an alkenyl-containing functional monomer and optionally an anhydride monomer;preferably, the content of the modified polypropylene (A) ranges from 20 wt % to 80 wt %, preferably from 30 wt % to 70 wt %, and more preferably from 35 wt % to 65 wt %, and the content of the low-modulus polypropylene (B) ranges from 20 wt % to 80 wt %, preferably from 30 wt % to 70 wt %, and more preferably from 35 wt % to 65 wt %, based on the total weight of the modified flexible polypropylene insulating material.
21. The method according to claim 20, comprising: S1: subjecting a reaction mixture A comprising homo- or co-polypropylene and a first unsaturated bond-containing polymerizable monomer to grafting reaction in the presence of an inert gas, to obtain a modified polypropylene;optionally, subjecting a reaction mixture B comprising a low-modulus polypropylene and a second unsaturated bond-containing polymerizable monomer to grafting reaction in the presence of an inert gas, to obtain a modified low-modulus polypropylene;S2: mixing the modified polypropylene with an unmodified low-modulus polypropylene and/or the modified low-modulus polypropylene and optional additives, and extruding and granulating to obtain the modified flexible polypropylene insulating material,preferably, the first unsaturated bond-containing polymerizable monomer and the second unsaturated bond-containing polymerizable monomer are each independently an alkenyl-containing functional monomer and optionally an anhydride monomer.
22. The method according to claim 21, wherein the reaction mixture A and the reaction mixture B each independently comprise a free radical initiator; the free radical initiator is selected from a peroxide-based free radical initiator and an azo-based free radical initiator; the peroxide-based radical initiator is preferably selected from at least one of dibenzoyl peroxide, dicumyl peroxide, di-tert-butyl peroxide, lauroyl peroxide, dodecyl peroxide, tert-butyl peroxybenzoate, diisopropyl peroxydicarbonate, tert-butyl peroxy (2-ethylhexanoate) and dicyclohexyl peroxydicarbonate; the azo-based radical initiator is preferably azobisisobutyronitrile and/or azobisisoheptonitrile.
23. The method according to claim 22, wherein the ratio of the mass of the radical initiator to the total mass of the unsaturated bond-containing polymerizable monomers ranges from 0.01:100 to 10:100, preferably from 0.5:100 to 6:100.
24. The method according to claim 21, wherein the mass ratio of the first unsaturated bond-containing polymerizable monomer to the homo- or co-polypropylene ranges from 0.5:100 to 35:100, preferably from 2:100 to 30:100, and more preferably from 2.5:100 to 25:100; the mass ratio of the second unsaturated bond-containing polymerizable monomer to the low-modulus polypropylene ranges from 0.1:100 to 20:100, preferably from 0.2:100 to 15:100, and more preferably from 0.5:100 to 10:100;when the unsaturated bond-containing polymerizable monomer includes an alkenyl-containing functional monomer and an anhydride monomer, the mass ratio of the alkenyl-containing functional monomer to the anhydride monomer ranges from 0.5:1 to 10:1 0.5-10:1, preferably from 2:1 to 8:1.
25. The method according to claim 21, wherein the temperature of the grafting reaction ranges from 30° C. to 130° C., and preferably from 60° C. to 120° C.; the time period of the grafting reaction ranges from 0.5 h to 10 h, and preferably from 1 h to 6 h.
26. The method according to claim 21, wherein the reaction mixture A and the reaction mixture B also each independently comprise at least one of the following components: a dispersant, an interfacial agent and an organic solvent, wherein the mass content of the dispersant ranges from 50% to 300% of the mass of the homo- or co-polypropylene/the low-modulus polypropylene, the mass content of the interfacial agent ranges from 1% to 30% of the mass of the homo- or co-polypropylene/the low-modulus polypropylene, and the mass content of the organic solvent ranges from 1% to 35% of the mass of the homo- or co-polypropylene/the low-modulus polypropylene.
27. The method according to claim 26, comprising: a. placing a homo- or co-polypropylene in a closed reactor, followed by inert gas replacement;b. adding a free radical initiator and a first unsaturated bond-containing polymerizable monomer to the closed reactor, and mixing with stirring;c. optionally adding an interfacial agent and optionally swelling the reaction system;d. optionally adding a dispersant, and heating the reaction system to the grafting reaction temperature, to carry out the grafting reaction;e. after the end of the reaction, optionally filtering, drying to obtain a modified polypropylene;f. mixing the modified polypropylene with ungrafted and/or grafted low-modulus polypropylene and optional aids, melt extruding and granulating, to obtain the modified flexible polypropylene insulating material;wherein, the preparation method of the grafted low-modulus polypropylene comprises:i. placing a low-modulus polypropylene in a closed reactor, followed by inert gas replacement;ii. adding a free radical initiator and a second unsaturated bond-containing polymerizable monomer to the closed reactor, and mixing with stirring;iii. optionally adding an interfacial agent and optionally swelling the reaction system;iv. optionally adding a dispersant, and heating the reaction system to the grafting reaction temperature, to carry out the grafting reaction;v. after the end of the reaction, optionally filtering, drying to obtain a modified low-modulus polypropylene.
28. The method according to claim 26, comprising: a. placing a homo- or co-polypropylene in a closed reactor, followed by inert gas replacement;b. mixing an organic solvent and a free radical initiator, and adding the mixture to the closed reactor;c. removing the organic solvent;d. adding a first unsaturated bond-containing polymerizable monomer, optionally adding an interfacial agent, and optionally swelling the reaction system;e. optionally adding a dispersant, and heating the reaction system to the grafting reaction temperature, to carry out the grafting reaction;f. after the end of the reaction, optionally filtering, drying to obtain a modified polypropylene;g. weighing the modified polypropylene, ungrafted and/or grafted low-modulus polypropylene, and optional aids in proportions, mixing, melt extruding and granulating, to obtain the modified flexible polypropylene insulating material;wherein the preparation method of the grafted low-modulus polypropylene comprises:i. placing a low-modulus polypropylene in a closed reactor, followed by inert gas replacement;ii. mixing an organic solvent and a free radical initiator, and adding the mixture to the closed reactor;iii. removing the organic solvent;iv. adding a second unsaturated bond-containing polymerizable monomer, optionally adding an interfacial agent, and optionally swelling the reaction system;v. optionally adding a dispersant, and heating the reaction system to the grafting reaction temperature, to carry out the grafting reaction;vi. after the end of the reaction, optionally filtering, drying to obtain a modified low-modulus polypropylene.
29. A cable, comprising the modified flexible polypropylene insulating material according to claim 1.

Priority Claims (3)

Number	Date	Country	Kind
202110892173.9	Aug 2021	CN	national
202110893165.6	Aug 2021	CN	national
202210876405.6	Jul 2022	CN	national

PCT Information

Filing Document	Filing Date	Country	Kind
PCT/CN2022/109917	8/3/2022	WO

MODIFIED FLEXIBLE POLYPROPYLENE INSULATING MATERIAL AND PREPARATION METHOD AND USE THEREOF

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Priority Claims (3)

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