USE OF POLYOLEFIN AS INSULATION MATERIAL

Description

[0001] The present invention relates to the field of polyolefins, in particular polyolefins which are used as insulating materials, e.g. in high-voltage technology.

[0002] Particularly in high-voltage engineering, cross-linked low-density polyolefins (mostly polyethylenes, so-called x-LDPE) are used because these materials are often characterized by low specific conductivity and high dielectric strength. However, a disadvantage in many applications is the undefined and rarely reproducible accumulation of space charge under static field loads, which makes it difficult to predict the space charge-induced field load during operation.

[0003] Oriented polyolefins are known from, among others, EP 3 098 059 A1, US 5 145 728 A, US 3 033 727 A, US 2013 / 288000 A1, EP 3 202 825 A1, EP 1 894 715 A1, US 2013 / 288000 A1 and EP 3 202 825 A1.

[0004] The task therefore arises to create polyolefins in which, in particular, space charge accumulation is improved or predictable.

[0005] This problem is solved by using a polyolefin according to claim 1. Accordingly, the use of a polyolefin as an insulating material is proposed, wherein the polyolefin is polyethylene having a degree of cross-linking between ≥ 0.01% and ≤ 4% and an orientation degree of ≥ 25%.

[0006] The degree of cross-linking will be determined by measuring the elastic modulus in the melt according to Neo-Hookean's theory of elasticity.

[0007] The degree of cross-linking xc is determined as follows via the Neo-Hooke equation, x c = M rep ⋅ E T ⋅ 100 % 2 1 − ν ⋅ ρ T ⋅ R ⋅ T where Mrep corresponds to the molecular weight of the repeating unit, E(T) to the storage modulus, v to the Poisson's ratio, p(T) to the density, R to the universal gas constant, and T to the absolute temperature. The degree of cross-linking is determined for T > Tm.

[0008] The orientation degree O will be determined using wide-angle X-ray diffraction (WAXS) and the evaluation of the crest of the diffraction reflections along the azimuthal angle. This is done by using the full width at half maximum (FWHM) of the intensity distribution of the considered peak in the WAXS diffraction pattern according to the formula O = (180° - H) / 180 * 100%.

[0009] According to a preferred embodiment, the degree of cross-linking of the polyolefin is between ≥ 0.1% and ≤ 2%.

[0010] According to a preferred embodiment, the degree of orientation of the polyolefin is between ≥ 40% and ≤ 100%, preferably ≥ 50%, even more preferably ≥ 60%.

[0011] According to a preferred embodiment, the polyolefin is selected from low-density polyethylene (LDPE), linear low-density polyethylene (LLDPE), and high-density polyethylene (HDPE).

[0012] According to a preferred embodiment, the polyolefin comprises LDPE and / or LLDPE, preferably it consists essentially of these.

[0013] For the purposes of the present invention, "essentially" means ≥ 95 wt%, more preferably ≥ 97 wt% and most preferably ≥ wt%.

[0014] According to a preferred embodiment, the average number-weighted molar mass M n of the polyolefin is ≥ 2,000 g / mol to ≤ 500,000 g / mol, particularly preferably ≥ 20,000 g / mol to ≤ 300,000 g / mol

[0015] According to a preferred embodiment, the melt flow index MFI (according to ISO 1133) of the polyolefin is ≥ 0.01 g / 10 min to ≤ 5 g / 10 min, particularly preferably ≥ 0.1 g / 10 min to ≤ 3 g / 10 min.

[0016] The polymer was produced using a process comprising the following steps: a) Preparation of a linear base polyolefin b) Optional crosslinking of the base polyolefin c) Stretching of the polyolefin d) Continuous cooling e) Isothermal crystallization

[0017] The individual steps of the method according to the invention are explained in more detail below, whereby individual features can be combined with one another as desired: Step a) Submitting a linear base polyolefin.

[0018] Preferred base polyolefins are in particular polyethylenes, especially low density polyethylene (LDPE), linear low density polyethylene (LLDPE), and high density polyethylene (HDPE).

[0019] According to a preferred embodiment, the average number-weighted molar mass M n of the base polyolefin is ≥ 2,000 g / mol to ≤ 500,000 g / mol, particularly preferably ≥ 20,000 g / mol to ≤ 300,000 g / mol.

[0020] According to a preferred embodiment, the melt flow index MFI (according to ISO 1133) of the base polyolefin is ≥ 0.01 g / 10 min to ≤ 5 g / 10 min, particularly preferably ≥ 0.1 g / 10 min to ≤ 3 g / 10 min.

[0021] The base polyolefin itself can be produced using all known methods from the state of the art. Step b) Networking (optional)

[0022] Step b) is carried out until a degree of cross-linking of ≥ 0.01% to ≤ 4%, preferably between ≥ 0.1% and ≤ 2%, is achieved. The degree of cross-linking can be adjusted, for example, by the ratio of base polyolefin to cross-linking reagent (see below).

[0023] Step b) is preferably carried out at elevated temperatures, particularly preferably temperatures from T m - 60°C to ≤ T m + 120°C, where T m is the melting temperature of the base polyolefin.

[0024] Step b) can be carried out using a solvent or without solvents.

[0025] Step b) is preferably carried out by adding a crosslinking reagent. This is understood to be a reagent that is able to react with the linear polyolefin strands of the base polyolefin and thus crosslink them.

[0026] Preferred crosslinking reagents are selected from the group containing peroxides, preferably dicumyl peroxide, di-tert-butyl peroxide, tert-butyl hydroperoxide, percarbonate, dibenzoyl peroxide Step c) Stretching

[0027] In step c), the polymer obtained in step a) or b) is preferably stretched by ≥ 5%, particularly preferably by ≥ 200%, most preferably by ≥ 300%, and preferably by ≤ 1500%.

[0028] Step c) can be performed either uniaxially or biaxially, depending on the application.

[0029] The term "uniaxial" means and / or includes, in particular, projections extending along one preferred direction. The term "biaxial" means and / or includes, in particular, projections extending along two preferred directions.

[0030] Step c) is preferably carried out at a strain rate of ≥0.1 % / min to ≤ 10000 % / min, preferably from ≥1 % / min to ≤ 1000 % / min.

[0031] Step c) is preferably carried out at a mechanical stress, based on the sample cross-section, of ≥0.001 MPa to ≤ 100 MPa, particularly preferably ≥0.1 MPa to ≤ 30 MPa. This has proven particularly effective in many applications.

[0032] According to a preferred embodiment of the invention, the polymer obtained in step b) is heated to a temperature preferably Tm - 60°C to ≤ Tm + 120°C, where Tm is the melting temperature of the base polyolefin in step a). It is then stretched.

[0033] According to the present invention, the method comprises a step d), which is carried out after step c): d) Continuous cooling or isothermal crystallization

[0034] In step d), the polymer is either cooled continuously, e.g. by contact with a cooling medium with a temperature of preferably ≥ 20°C to ≤ T m - 20°C, or preferably crystallized isothermally at a temperature between 20°C and T m - 5°C.

[0035] According to the present invention, the method comprises a step e), which is carried out after step c) and / or d): e) Isothermal crystallization

[0036] In step e), the polymer is preferably crystallized isothermally at a temperature between 20°C and Tm - 5°C.

[0037] The present invention relates to the use of a polyolefin according to the invention as an insulating material, in particular in High-voltage applications, cable manufacturing, dielectric in capacitor applications

[0038] The aforementioned components, as well as those claimed and described in the exemplary embodiments, to be used according to the invention, are not subject to any special exceptional conditions with regard to their size, shape, material selection and technical concept, so that the selection criteria known in the field of application can be applied without restriction.

[0039] Further details, features and advantages of the subject matter of the invention will become apparent from the dependent claims and from the following description of the associated drawings, in which several embodiments of the polymer and the method according to the invention are shown by way of example.

[0040] LDPE was mixed with approximately 0.2% dicumyl peroxide (DCP) in an extruder at a temperature of 130 °C, resulting in a cross-linking of 0.13%.

[0041] The extrudate was then pressed into 500 µm thick films in a hot press at a temperature of 180 °C using spacers and crosslinked by 20 minutes of tempering. To orient the resulting crosslinked LDPE films, they were tempered on a 160 °C hot plate and then stretched to relative strains of 100 to 900% (or degrees of stretch λ of 2 to 10) and subsequently crystallized on a second hot plate at a temperature of 80 °C.

[0042] The electrical properties of the cross-linked LDPE films were subsequently determined using an LCR meter and a pulsed electroacoustic method. To evaluate the space charge accumulation, a DC electric field ≤ 40 kV / mm was applied for load times ≥ 3000 s, and the amount of stored space charge was then determined.

[0043] The following table shows the results achieved: Stretch ratio λ O Permittivity ε r Stored space charge amount N / N max 1 0 2,3 1 2 61,33 2,13 0,62-0,80 3 66,66 4 81,22 2,09 0,45-0,63 5 87,89 6 87,55 1,96 <0,4 7 92 8 93,3 1,87 <0,4 9 96,67 10 98,89 1,95 <0,4

[0044] The individual combinations of components and features of the embodiments already mentioned are exemplary; the exchange and substitution of these teachings with other teachings contained in this publication and with the cited publications are also expressly considered. The person skilled in the art recognizes that variations, modifications, and other embodiments described herein may also occur without deviating from the inventive concept and scope of the invention. Accordingly, the above description is exemplary and not to be considered limiting. The word "comprise" used in the claims does not exclude other components or steps. The indefinite article "a" does not preclude the meaning of a plural. The mere fact that certain dimensions are cited in mutually different claims does not indicate that a combination of these dimensions cannot be used to advantage.The scope of the invention is defined in the following claims and their equivalents.

Claims

1. Use of a polyolefin, wherein the polyolefin is polyethylene having a degree of cross-linking between ≥ 0.01% and ≤ 4% and an orientation degree of ≥ 25%, as an insulation material, wherein the polyolefin being produced by a process comprising the steps: a) Presentation of a linear base polyolefin b) Optional crosslinking of the base polyolefin c) Stretching the polymer d) Continuous cooling e) Isothermal crystallisation, wherein the degree of cross-linking xc was determined according to the following equation: x c = M rep ⋅ E T ⋅ 100 % 2 1 − ν ⋅ ρ T ⋅ R ⋅ T wherein Mrep corresponds to the molecular weight of a repeating unit, E(T) to the storage modulus, v to the Poisson's ratio, p(T) to the density, R to the universal gas constant and T to the absolute temperature, wherein T > Tm and Tm is the melting temperature of the base polyolefin, and wherein the degree of orientation O was determined by wide-angle X-ray diffractometry from the half-width H of the intensity distribution of the diffraction reflections along the azimuthal angle according to the following formula: O = 180 ° − H / 180 * 100 % .

2. Use according to claim 1, wherein the polyolefin is selected from Low Density Polyethylene (LDPE), Linear Low-Density Polyethylene (LLDPE), and High-Density Polyethylene (HDPE).

3. Use according to any one of claims 1 to 2, wherein the degree of orientation of the polyolefin is between ≥ 40% and ≤ 100%4. Use according to any one of claims 1 to 3, wherein the average number-weighted molar mass of the polyolefin is ≥ 2,000 g / mol to ≤ 500,000 g / mol5. Use according to any one of claims 1 to 4, wherein the melt flow index MFI (according to ISO 1133) of the polyolefin is from ≥ 0.01 g / 10min to ≤ 5 g / 10min.

6. Use according to any one of claims 1 to 5, wherein the average molar mass of the base polyolefin is ≥ 2,000 g / mol to ≤ 300,000 g / mol.

7. Use according to any one of claims 1 to 6, wherein the melt flow index MFI (according to ISO 1133) of the base polyolefin is from ≥ 0.01 g / 10min to ≤ 5 g / 10min.

8. Use according to any one of claims 1 to 7, wherein in step (c) the polymer obtained in step (a) or (b) was stretched by ≥ 5% to ≤1500%.

9. Use according to any one of claims 1 to 8, wherein step (c) is carried out at a strain rate of ≥0.1 % / min to ≤ 10000% / min.

10. Use according to any one of claims 1 to 9, wherein step (b) was preferably carried out at a temperature in a range of Tm - 60°C to ≤ Tm + 120 °C.

11. Use according to any one of claims 1 to 10, wherein in step (e) the polymer is preferably crystallised isothermally at a temperature between 20°C and Tm - 5°C.