Ultrahigh molecular weight polyethylene fiber containing multi-branched filler, and manufacturing method and application thereof
By introducing multi-branched fillers into ultra-high molecular weight polyethylene fibers and performing modification treatment, the contradiction between the anti-cut performance of gloves and the wearable comfort is solved, and a high-strength, high-strength, and high-strength, and safe fiber material is achieved.
Patent Information
- Application Number
- CN202311153914.7
- Authority / Receiving Office
- CN · China
- Patent Type
- Applications(China)
- Current Assignee / Owner
- Filing Date
- 2023-09-08
- Publication Date
- 2025-03-11
- Estimated Expiration
- 2043-09-08
AI Technical Summary
The existing ultra-high molecular weight polyethylene fiber gloves are difficult to take into account between cutting resistance and wear comfort, and the fibrous filler is prone to take off, resulting in pollution and secondary damage to the production environment.
Multi-branched fillers (such as whiskers) are introduced into ultra-high molecular weight polyethylene fibers, and the surface chemical modification and physical modification treatment ensures that the fillers are evenly dispersed and stable in the fibers.
It improves the cutting resistance of the fabric and reaches EN388-2003 standard level 5, while improving wearable comfort and safety, reducing pollution and secondary damage caused by filler removal.
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Abstract
Description
Technical Field
[0001] The present invention relates to the technical field of fiber manufacturing, and more specifically to an ultra-high molecular weight polyethylene fiber containing multi-branched fillers, a manufacturing method thereof and an application thereof. Background Art
[0002] Ultra-high molecular weight polyethylene fiber (UHMWPE) is the fiber with the highest specific strength and specific modulus in the world. It is a fiber spun from polyethylene with a molecular weight of 1 million to 5 million. Ultra-high molecular weight polyethylene fiber is the fiber with the highest specific strength among the currently industrialized fiber materials. It has excellent properties such as high strength, high modulus, wear resistance, and chemical corrosion resistance. It is widely used in safety protection, military, aerospace, ocean, sports and other fields. With the continuous deepening of military-civilian integration, the application of ultra-high molecular weight polyethylene fiber in the civilian market has gradually increased, among which the civilian market dominated by anti-cut gloves has gradually occupied a dominant position. At present, the highest cutting grade of protective gloves made of commonly used ultra-high molecular weight polyethylene fibers is EN388-2016 standard level 3, which does not meet the needs of protection against cut hazards in actual working environments.
[0003] In order to improve the anti-cutting grade of gloves, a common method is to blend steel wire materials with ultra-high molecular weight polyethylene fibers to improve the anti-cutting grade. Although this method can improve the anti-cutting performance of gloves, it is difficult to wear and has poor comfort because the steel wire is relatively hard and cannot achieve compatibility between protective performance and comfort performance. At present, the common method is to add fibrous fillers to fill and modify UHMWPE.
[0004] Patent CN101528998A discloses a composite yarn containing silk threads or fixed-length fibers, wherein the fixed-length fibers used are short-cut hard fibers with a certain aspect ratio, including glass fibers, mineral fibers or metal fibers, which are used to improve the cutting resistance of the yarn.
[0005] Patent CN109610040A discloses pouring glass fiber into a first white oil and mixing to obtain a glass fiber premix, then mixing the glass fiber premix, an antioxidant and UHMWPE powder in a second white oil to obtain a spinning mixture, which is swollen and extruded to form a molten state, cooled to form a gel filament and obtain a composite fiber. Summary of the invention
[0006] The inventors of the present invention have found that although the cut resistance coefficient of gloves can be improved by adding fibrous fillers to fill and modify UHMWPE, the gloves feel hard to wear, and because the fibrous fillers are easily removed from the fiber matrix during the manufacturing process or use, the production environment is polluted, or secondary damage such as itching and allergies are caused to the user, and the protection performance and wearing comfort (especially wearing safety) cannot be unified. To this end, the inventors of the present invention have found through hard research that these technical problems existing in the prior art can be solved by introducing specific multi-branched fillers (especially whiskers) into the ultra-high molecular weight polyethylene matrix. The present invention is completed based on this discovery.
[0007] Specifically, the present invention relates to the following aspects.
[0008] 1. An ultra-high molecular weight polyethylene fiber, comprising ultra-high molecular weight polyethylene as a matrix and a multi-branched filler (such as whiskers) dispersed in the matrix, wherein the multi-branched filler has a plurality of (preferably at least 2, more preferably 2-10 or 3-8) dendrites in its structure, and the plurality of dendrites are the same or different from each other, and the length (calculated from the root) is independently 5-2000 μm (preferably 10-300 μm).
[0009] 2. The fiber described in any of the preceding or following aspects, wherein the content of the multi-branched filler is no more than 30 parts by weight (preferably 5-12 parts by weight) relative to 100 parts by weight of the ultra-high molecular weight polyethylene.
[0010] 3. The fiber described in any of the preceding or following aspects, wherein the viscosity-average molecular weight of the ultra-high molecular weight polyethylene is 1 million to 9 million (preferably 3 million to 5 million).
[0011] 4. The fiber according to any one of the preceding or following aspects, wherein the plurality of dendrites are identical or different from each other, and each independently has a diameter (root) of at most 10 μm (preferably 0.05-3 μm).
[0012] 5. The fiber described in any of the preceding or following aspects, wherein the multi-branched filler is substantially uniformly dispersed in the matrix, or, there is substantially no agglomerated structure of the multi-branched filler in the matrix, or, the minimum distance between any two adjacent multi-branched fillers in the matrix is greater than 0.1 μm (preferably greater than 5 μm).
[0013] 6. The fiber described in any one of the preceding or following aspects, wherein the multi-branched filler is selected from at least one of inorganic compound whiskers and organic compound whiskers, preferably at least one of inorganic compound whiskers.
[0014] 7. The fiber described in any of the preceding or following aspects, wherein the inorganic compound is at least one selected from inorganic oxygen-containing compounds, preferably at least one selected from metal oxides, metal hydroxides and metal oxygenates, in particular at least one selected from metal oxygenates, such as at least one selected from silicon carbide, silicon nitride, aluminum oxide, zinc oxide, magnesium oxide, calcium carbonate, basic magnesium sulfate, aluminum borate, magnesium borate, potassium titanate and calcium sulfate; or, the organic compound is at least one selected from organic polymers, preferably at least one selected from cellulose, polyester, polyamide, poly 4-hydroxybenzoate (PHB).
[0015] 8. The fiber described in any one of the preceding or following aspects, wherein the multi-branched filler has been subjected to surface chemical modification, such as surface chemical modification with a silane coupling agent.
[0016] 9. The fiber described in any of the preceding or following aspects, wherein the silane coupling agent is at least one selected from aminopropyltriethoxysilane, γ-(glycidyloxy)propyltrimethoxysilane, and γ-(methacryloyloxy)propyltrimethoxysilane.
[0017] 10. The fiber according to any one of the preceding or following aspects, wherein the multi-branched filler has been subjected to a surface physical modification treatment, such as a surface roughening treatment and / or a surface polymer coating treatment.
[0018] 11. The fiber described in any of the preceding or following aspects, wherein the polymer is selected from at least one of thermoplastic polymers, thermosetting polymers and rubbers, and preferably selected from at least one of cellulose esters, olefin polymers (polyvinyl acetate, polyvinyl alcohol, perchlorethylene, polyisobutylene, etc.), polyesters, polyethers, polyamides, polyacrylates, α-cyanoacrylates, polyvinyl acetals, ethylene-vinyl acetate copolymers and isocyanates.
[0019] 12. The fiber described in any of the preceding or following aspects, wherein the angle between any two adjacent dendrites is greater than 5° (preferably 30°-90°).
[0020] 13. The fiber according to any one of the preceding or following aspects, wherein the single filament fineness is at least 0.5 dtex (preferably 0.9-5 dtex, most preferably 1-3 dtex).
[0021] 14. A method for producing ultra-high molecular weight polyethylene fiber, comprising the following steps:
[0022] 1) optionally subjecting a multi-branched filler (such as whiskers) to a surface chemical modification and / or surface physical modification to obtain a modified multi-branched filler, wherein the multi-branched filler has a plurality of (preferably at least 2, more preferably 2-10 or 3-8) dendrites in its structure, and the plurality of dendrites are identical or different to each other, and the length (calculated from the root) of each independently ranges from 5 to 2000 μm (preferably 10 to 300 μm),
[0023] 2) mixing the modified multi-branched filler or the multi-branched filler, ultra-high molecular weight polyethylene and a solvent to obtain a spinning solution,
[0024] 3) Spinning the spinning solution into the polyethylene fiber.
[0025] 15. The manufacturing method described in any of the above or the following aspects, wherein before performing the step 1), it also includes a step of drying the multi-branched filler, and the drying includes: reducing pressure, a drying temperature of 80-200°C (preferably 90-120°C), and a drying time of 0.5-10h (preferably 1-4h).
[0026] 16. The manufacturing method described in any of the above or the following aspects, wherein the surface chemical modification treatment includes: using a silane coupling agent, the amount of the silane coupling agent is 0.8-5wt% (preferably 1-3wt%) of the weight of the multi-branched filler, the treatment temperature is 40-100°C (preferably 70-90°C), and the treatment time is 1-120min (preferably 5-30min).
[0027] 17. The manufacturing method described in any of the above or below aspects, wherein the surface physical modification treatment includes: using a polymer for surface coating, the amount of the polymer used (dry basis) is at least 1%wt% (preferably 5-10wt%) of the weight of the multi-branched filler, the treatment temperature is at least 30°C (preferably 40-60°C), and the treatment time is at least 1 min (preferably 5-10 min).
[0028] 18. The manufacturing method described in any of the preceding or subsequent aspects, wherein the amount of the multi-branched filler or the modified multi-branched filler (calculated as multi-branched filler) is at most 50 parts by weight (preferably 6-12 parts by weight) relative to 100 parts by weight of the ultra-high molecular weight polyethylene, and the amount of the solvent is at least 500 parts by weight (preferably 1000-2000 parts by weight).
[0029] 19. The manufacturing method described in any of the above or the following aspects, wherein in step 3), the spinning comprises: a gel spinning method, a primary stretching ratio of the spinneret is 3-10, a super stretching temperature is 80-150°C, and a super stretching ratio is 6-20 (preferably 8-15).
[0030] 20. The manufacturing method described in any of the above or the following aspects, wherein in step 3), it also includes a step of combing and orienting the spinning solution.
[0031] 21. A fabric comprising the ultra-high molecular weight polyethylene fiber described in any one of the preceding or following aspects or the ultra-high molecular weight polyethylene fiber produced by the production method described in any one of the preceding or following aspects.
[0032] 22. The fabric described in any one of the preceding or following aspects has a cut resistance performance reaching level 5 of EN388-2003 standard.
[0033] 23. The fabric described in any one of the preceding or following aspects further comprises at least one other fiber selected from natural plant fibers, natural animal fibers, artificial regenerated fibers, synthetic fibers and inorganic fibers.
[0034] Technical Effects
[0035] The multi-branched filler used in the present invention is different from the fibrous filler in the prior art. It can produce an anchoring effect in the fiber, and can exist in the fiber more stably without being easily dislodged, thereby effectively reducing secondary damage to the human body. In particular, during the fiber manufacturing process or the cutting process, the branch-like protrusion structure of the multi-branched filler can remain stable without being dislodged or rolling. In addition, the branch-like protrusion structure of the multi-branched filler can simultaneously bridge both sides of the crack to organize the crack expansion, thereby achieving high strength and high toughness and having anti-cutting performance effects.
[0036] The ultra-high molecular weight polyethylene fiber of the invention can greatly improve the wearing comfort of the fabric, especially the wearing safety, and the fabric can reach level 5 of the cut resistance EN388-2003 standard. BRIEF DESCRIPTION OF THE DRAWINGS
[0037] Figure 1 Schematic diagram of the dispersion of the multi-branched filler in the polyethylene matrix according to the present invention.
[0038] exist Figure 1 In the figure, H represents the length of the dendrite (measured from the root), and L represents the minimum distance between two adjacent multi-branched fillers. DETAILED DESCRIPTION
[0039] The specific embodiments of the present invention are described in detail below, but it should be pointed out that the protection scope of the present invention is not limited by these specific embodiments, but is determined by the claims in the appendix.
[0040] All publications, patent applications, patents and other references mentioned in this specification are incorporated herein by reference. Unless otherwise defined, all technical and scientific terms used in this specification have the meanings conventionally understood by those skilled in the art. In the event of a conflict, the definitions in this specification shall prevail.
[0041] When this specification uses the prefix "well-known to those skilled in the art", "prior art" or similar terms to introduce materials, substances, methods, steps, devices or components, etc., the objects introduced by the prefix cover those commonly used in the art when this application is filed, but also include those that are not commonly used at present but will become recognized in the art as being suitable for similar purposes.
[0042] In the context of this specification, by substantially it is meant a deviation of no more than 20%, preferably no more than 10%, 5% or 1%.
[0043] In the context of this specification, the removal of filler from the fiber matrix is characterized by the degree of material shedding from the fiber during the fiber manufacturing process.
[0044] In the context of this specification, the agglomeration is measured as follows: a 10 cm long section is randomly cut from the fiber, the number of agglomerated structures is investigated under a laser microscope, and then scored according to the following criteria. The measurement is repeated 10 times and the average value is taken.
[0045] No reunion: 0,
[0046] Small amount of reunion: less than 2,
[0047] Medium reunion: 3-4,
[0048] Large gatherings: 5 or more.
[0049] In the context of this specification, the linear density deviation rate is measured according to GB / T 14343.
[0050] In the context of this specification, the distance between two fillers or similar expressions means the distance between any point on one filler and any point on the other filler.
[0051] Unless otherwise specified, all percentages, parts, ratios, etc. mentioned in this specification are based on weight and pressure is gauge pressure.
[0052] In the context of this specification, there are no specific operating conditions, additives, etc., and those known in the art are directly applicable without particular limitation.
[0053] In the context of this specification, any two or more embodiments of the present invention may be arbitrarily combined, and the technical solutions thus formed belong to part of the original disclosure of this specification and also fall within the protection scope of the present invention.
[0054] According to one embodiment of the present invention, it relates to an ultra-high molecular weight polyethylene fiber. The ultra-high molecular weight polyethylene fiber is generally a monofilament or a filament.
[0055] According to one embodiment of the present invention, the ultra-high molecular weight polyethylene fiber comprises ultra-high molecular weight polyethylene as a matrix and a multi-branched filler (such as whisker) dispersed in the matrix. According to the present invention, the multi-branched filler, especially the whisker, can be directly purchased from the market or manufactured according to conventional methods known in the relevant technical field, and there is no particular limitation except for the relevant content below.
[0056] According to one embodiment of the present invention, the multi-branched filler has a plurality of branch-like protrusions in its structure. Preferably, the number of the branch-like protrusions is at least 2, more preferably 2-10 or 3-8. When the number of branch-like protrusions is too large, the multi-branched filler produces a local mass concentration point in the fiber matrix, and the linear density uniformity of the ultra-high molecular weight polyethylene fiber along the length direction is too poor (the linear density deviation rate is too large), which may have an adverse effect on the processing performance, and the cutting resistance may be insufficient. In addition, when the number of branch-like protrusions is too small, the risk of the multi-branched filler escaping from the fiber matrix increases, and the cutting resistance may be insufficient.
[0057] According to the present invention, the Mohs hardness of the multi-branched filler is greater than the Mohs hardness of the ultra-high molecular weight polyethylene. For this reason, the multi-branched filler is sometimes also called a hard multi-branched filler.
[0058] According to one embodiment of the present invention, the plurality of branch-like protrusions are identical or different from each other, and the length (calculated from the root) is independently 5-2000 μm (preferably 10-300 μm). When the length of the branch-like protrusion is too small, the cut resistance of the fiber may be insufficient, and the risk of the multi-branched filler escaping from the fiber matrix increases. In addition, when the length of the branch-like protrusion is too large, the multi-branched filler produces a local mass concentration point in the fiber matrix, and the uniformity of the linear density of the ultra-high molecular weight polyethylene fiber along the length direction is too poor, which may have an adverse effect on the processing performance, and the cut resistance may be insufficient. Moreover, when the length of the branch-like protrusion is too large, the multi-branched filler is easy to form an agglomerated structure in the fiber matrix, which may cause the uniformity of the fiber linear density to deteriorate, affecting the wearing comfort.
[0059] According to one embodiment of the present invention, the content of the multi-branched filler is no more than 30 parts by weight (preferably 5-12 parts by weight) relative to 100 parts by weight of the ultra-high molecular weight polyethylene. When the content of the multi-branched filler is too low, the cutting resistance of the fiber may be insufficient. In addition, when the content of the multi-branched filler is too high, the multi-branched filler is prone to form an agglomeration structure in the fiber matrix, which may cause the uniformity of the fiber line density to deteriorate, affecting the wearing comfort.
[0060] According to one embodiment of the present invention, the viscosity-average molecular weight of the ultra-high molecular weight polyethylene is 1 million to 9 million (preferably 3 million to 5 million).
[0061] According to one embodiment of the present invention, the plurality of dendrites are identical to or different from each other, and each independently has a diameter (root) of at most 10 μm (preferably 0.05-3 μm).
[0062] According to one embodiment of the present invention, the multi-branched filler is substantially uniformly dispersed in the matrix. In other words, there is substantially no agglomerate structure of the multi-branched filler in the matrix. Here, the so-called agglomerate structure refers to a composite structure formed by entanglement or interweaving of multiple multi-branched fillers. As a quantitative indicator, the minimum distance between any two adjacent multi-branched fillers in the matrix is greater than 0.1 μm (preferably greater than 5 μm). According to the present invention, when the multi-branched filler forms an agglomerate structure in the fiber matrix, it may cause the uniformity of the fiber line density to deteriorate, affecting the wearing comfort.
[0063] According to one embodiment of the present invention, the multi-branched filler is selected from at least one of inorganic compound whiskers and organic compound whiskers, preferably selected from at least one of inorganic compound whiskers.
[0064] According to one embodiment of the present invention, the inorganic compound is at least one selected from inorganic oxygen-containing compounds, preferably at least one selected from metal oxides, metal hydroxides and metal oxyacid salts, in particular at least one selected from metal oxyacid salts, such as at least one selected from silicon carbide, silicon nitride, aluminum oxide, zinc oxide, magnesium oxide, calcium carbonate, basic magnesium sulfate, aluminum borate, magnesium borate, potassium titanate and calcium sulfate.
[0065] According to one embodiment of the present invention, the organic compound is at least one selected from organic polymers, preferably at least one selected from cellulose, polyester, polyamide, and poly 4-hydroxybenzoate (PHB).
[0066] According to one embodiment of the present invention, it is preferred that the multi-branched filler undergoes surface chemical modification, such as surface chemical modification with a silane coupling agent. Without surface chemical modification, the anchoring effect of the multi-branched filler on the fiber matrix may deteriorate, the risk of the multi-branched filler escaping from the fiber matrix increases, and the cutting resistance may be insufficient.
[0067] According to one embodiment of the present invention, the silane coupling agent is selected from at least one of aminopropyltriethoxysilane, γ-(glycidyloxy)propyltrimethoxysilane and γ-(methacryloyloxy)propyltrimethoxysilane.
[0068] According to one embodiment of the present invention, the multi-branched filler is subjected to a surface physical modification treatment, such as a surface roughening treatment and / or a surface polymer coating treatment.
[0069] According to one embodiment of the present invention, the polymer is selected from at least one of thermoplastic polymers, thermosetting polymers and rubbers, preferably selected from at least one of cellulose esters, olefin polymers (polyvinyl acetate, polyvinyl alcohol, perchlorethylene, polyisobutylene, etc.), polyesters, polyethers, polyamides, polyacrylates, a-cyanoacrylates, polyvinyl acetals, ethylene-vinyl acetate copolymers and isocyanates.
[0070] According to one embodiment of the present invention, the angle between any two adjacent branch-like protrusions is greater than 5° (preferably 30-90°). When the angle is too small, the fiber matrix may not be sufficiently impregnated with the multi-branched filler, resulting in an increased risk of the multi-branched filler escaping from the fiber matrix, and the cutting resistance may be insufficient. In addition, when the angle is too large, the anchoring effect of the multi-branched filler on the fiber matrix may deteriorate, the risk of the multi-branched filler escaping from the fiber matrix increases, and the cutting resistance may be insufficient.
[0071] According to one embodiment of the present invention, the fiber has a single filament fineness of at least 0.5 dtex (preferably 0.9-5 dtex, most preferably 1-3 dtex).
[0072] According to one embodiment of the present invention, it also relates to a method for manufacturing an ultra-high molecular weight polyethylene fiber. According to the present invention, the manufacturing method can be used to manufacture the ultra-high molecular weight polyethylene fiber of the present invention as described above. For this reason, the contents not described or expanded in detail in this document for the manufacturing method can be directly applied to the contents given in the previous text of this specification for the ultra-high molecular weight polyethylene fiber, and will not be repeated here.
[0073] According to one embodiment of the present invention, the method for producing the ultra-high molecular weight polyethylene fiber comprises the following steps:
[0074] 1) optionally subjecting a multi-branched filler (such as whiskers) to a surface chemical modification and / or a surface physical modification to obtain a modified multi-branched filler,
[0075] 2) mixing the modified multi-branched filler or the multi-branched filler, ultra-high molecular weight polyethylene and a solvent to obtain a spinning solution,
[0076] 3) Spinning the spinning solution into the polyethylene fiber.
[0077] According to one embodiment of the present invention, before performing step 1), the method further comprises the step of drying the multi-branched filler.
[0078] According to one embodiment of the present invention, the drying comprises: a drying temperature of 80-200° C. (preferably 90-120° C.) and a drying time of 0.5-10 h (preferably 1-4 h).
[0079] According to one embodiment of the present invention, the surface chemical modification treatment includes: using a silane coupling agent, the amount of the silane coupling agent is 0.8-5wt% (preferably 1-3wt%) of the weight of the multi-branched filler, the treatment temperature is 40-100°C (preferably 70-90°C), and the treatment time is 1-120min (preferably 5-30min). Without the surface chemical modification treatment, the anchoring effect of the multi-branched filler on the fiber matrix may deteriorate, the risk of the multi-branched filler escaping from the fiber matrix increases, and the cutting resistance may be insufficient.
[0080] According to one embodiment of the present invention, the surface physical modification treatment comprises: using a polymer for surface coating, the amount of the polymer (dry basis) is at least 1%wt% (preferably 5-10wt%) of the weight of the multi-branched filler, the treatment temperature is at least 30°C (preferably 40-60°C), and the treatment time is at least 1min (preferably 5-10min).
[0081] According to one embodiment of the present invention, relative to 100 parts by weight of the ultra-high molecular weight polyethylene, the amount of the multi-branched filler or the modified multi-branched filler (calculated as multi-branched filler) is at most 50 parts by weight (preferably 6-12 parts by weight), and the amount of the solvent is at least 500 parts by weight (preferably 1000-2000 parts by weight).
[0082] According to one embodiment of the present invention, in step 3), the spinning adopts a gel spinning method, including swelling at 60-120°C for 1-3h, dissolving by screw shearing, the dissolving temperature is 180-250°C, extruding the spinning gel, and then spinning through a spinneret. Preferably, under the condition of keeping warm at 100-200°C, flowing through a whisker comber, the whiskers are oriented and arranged in the direction of the spinning solution flow. In addition, the primary stretching ratio of the spinneret is 3-10, the super stretching temperature is 80-150°C, and the super stretching ratio is 6-20 (preferably 8-15).
[0083] The ultra-high molecular weight polyethylene fiber of the present invention can be made into cut-resistant fabrics, including but not limited to at least one of woven fabrics, knitted fabrics, non-woven fabrics, and non-woven fabrics, and its cut resistance reaches level 5 of EN388-2016 standard.
[0084] According to one embodiment of the present invention, the fabric further comprises at least one other fiber selected from natural plant fibers, natural animal fibers, artificial regenerated fibers, synthetic fibers and inorganic fibers.
[0085] Example
[0086] The present invention is further described in detail below using examples, but the present invention is not limited to these examples.
[0087] Example 1
[0088] The ultra-high molecular weight polyethylene fiber of this embodiment comprises ultra-high molecular weight polyethylene as a matrix and multi-branched fillers dispersed in the matrix.
[0089] In this embodiment, the multi-branched filler is a whisker, which is a 1:1 mixture of zinc oxide and calcium sulfate by mass. Its surface is treated with γ-(glycidyloxy)propyltrimethoxysilane and has 4-7 dendrites. The length of each dendrite (from the root) is between 100-200 μm, the diameter (root) is between 0.5-1 μm, and the angle between any two adjacent dendrites is between 40-60 degrees.
[0090] In this embodiment, the content of the whiskers is 8 parts by weight relative to 100 parts by weight of the ultra-high molecular weight polyethylene. The viscosity average molecular weight of the ultra-high molecular weight polyethylene is 4 million.
[0091] In this embodiment, 10 cm of ultra-high molecular weight polyethylene fiber was observed with a laser microscope and it was found that the whiskers were basically evenly dispersed in the matrix, no agglomeration structure of the whiskers was observed in the matrix, and the minimum distance between any two adjacent whiskers in the matrix was greater than 100 μm.
[0092] In this embodiment, after measurement, the single fiber fineness of the ultra-high molecular weight polyethylene fiber is 2.5 dtex.
[0093] The method for producing ultra-high molecular weight polyethylene fibers is as follows.
[0094] The whiskers are treated with the silane coupling agent to prepare modified whiskers, and then the modified whiskers, ultra-high molecular weight polyethylene and solvent decalin are mixed to obtain a spinning solution, and the spinning solution is spun into polyethylene fiber. Wherein, before the silane coupling agent treatment, the whiskers are dried at a drying temperature of 100° C. and a drying time of 3 hours. The amount of the silane coupling agent is 2wt% of the whisker weight, the treatment temperature is 80° C., and the treatment time is 20 minutes. During the mixing process, 100 parts by weight of ultra-high molecular weight polyethylene, 9 parts by weight of the modified whiskers (in terms of whiskers), and 1500 parts by weight of the solvent are used. The gel spinning method is adopted, the primary stretching ratio of the spinneret is 8, the super-stretching temperature is 145° C., and the super-stretching ratio is 10. The spinning solution passes through a combing orientation zone before spinning.
[0095] Ultra-high molecular weight polyethylene fibers were coated with spandex and then knitted into gloves on a 13-needle glove loom for EN388-2016 cut resistance test.
[0096] Example 2
[0097] Compared with Example 1, no silane coupling agent treatment was performed. The single fiber fineness of the ultra-high molecular weight polyethylene fiber of this example was 2.9 dtex.
[0098] Example 3
[0099] Compared with Example 1, the whiskers are a mixture of magnesium oxide, magnesium borate, potassium titanate in a mass ratio of 1:1:1, and the whiskers have 15-20 dendrites, each with a length (from the root) of 30-120 μm and a diameter (from the root) of 1-2 μm. The single filament fineness of the ultra-high molecular weight polyethylene fiber of this example is 2.7 dtex.
[0100] Example 4
[0101] Compared with Example 1, the whiskers are cellulose whiskers with 2-3 dendrites, each with a length (from the root) of 200-300 μm and a diameter (from the root) of 0.1-0.5 μm. The single filament fineness of the ultra-high molecular weight polyethylene fiber of this example is 1.9 dtex.
[0102] Example 5
[0103] Compared with Example 1, the amount of modified whiskers (calculated as whiskers) used is 40 parts by weight for 100 parts by weight of ultra-high molecular weight polyethylene. The single-filament fineness of the ultra-high molecular weight polyethylene fiber of this example is 2.2 dtex.
[0104] Example 6
[0105] Compared with Example 1, the length of each dendrite (calculated from the root) is between 1500-2000 μm. The single fiber fineness of the ultra-high molecular weight polyethylene fiber of this example is 2.3 dtex.
[0106] Example 7
[0107] Compared with Example 1, the diameter (root) of each dendrite is between 15 and 20 μm. The single fiber fineness of the ultra-high molecular weight polyethylene fiber of this example is 2.2 dtex.
[0108] Example 8
[0109] Compared with Example 1, the angle between any two adjacent dendrites is between 120 and 160 degrees. The single fiber fineness of the ultra-high molecular weight polyethylene fiber of this example is 2.5 dtex.
[0110] Example 9
[0111] Compared with Example 1, the angle between any two adjacent dendrites is between 10 and 25 degrees. The single fiber fineness of the ultra-high molecular weight polyethylene fiber of this example is 2.5 dtex.
[0112] Example 10
[0113] Compared with Example 1, only the whisker surface treatment form is changed, and polyacrylate is used for coating. The single fiber fineness of the ultra-high molecular weight polyethylene fiber in this example is 2.5 tex.
[0114] Embodiment 11
[0115] Compared with Example 1, the super-drawing ratio is 5. The single-filament fineness of the ultra-high molecular weight polyethylene fiber of this example is 1.2 dtex.
[0116] Comparative Example 1
[0117] The fiber is commercially available LY25 ultra-high molecular weight polyethylene fiber, which does not contain whiskers. The single fiber fineness of the ultra-high molecular weight polyethylene fiber of this comparative example is 1.2 dtex.
[0118] Comparative Example 2
[0119] Compared with Example 1, whiskers are not added but glass micro beads with a diameter of 1 μm are used instead. The single fiber fineness of the ultra-high molecular weight polyethylene fiber of this comparative example is 1.9 dtex.
[0120] Comparative Example 3
[0121] Compared with Example 1, whiskers are not added, but glass fibers are used instead, which have no branches, a diameter of 5 μm, and an aspect ratio of 30 to 50. The single-filament fineness of the ultra-high molecular weight polyethylene fiber of this comparative example is 1.9 dtex.
[0122] Comparative Example 4
[0123] Compared with Example 1, the length of each dendrite (calculated from the root) is between 2500-3000 μm. The single fiber fineness of the ultra-high molecular weight polyethylene fiber of this comparative example is 2.3 dtex.
[0124]
Claims
1. An ultra-high molecular weight polyethylene fiber, comprising ultra-high molecular weight polyethylene as a matrix and a multi-branched filler (such as whiskers) dispersed in the matrix, wherein the multi-branched filler has a plurality of (preferably at least 2, more preferably 2-10 or 3-8) dendrites in its structure, and the plurality of dendrites are the same or different from each other, and the length (calculated from the root) is independently 5-2000 μm (preferably 10-300 μm).
2. The fiber of claim 1, wherein the content of the multi-branched filler is no more than 30 parts by weight (preferably 5-12 parts by weight) relative to 100 parts by weight of the ultra-high molecular weight polyethylene.
3. The fiber of claim 1, wherein the viscosity-average molecular weight of the ultra-high molecular weight polyethylene is 1 million to 9 million (preferably 3 million to 5 million).
4. The fiber of claim 1, wherein the plurality of dendrites are identical to or different from each other, and each independently has a diameter (root) of at most 10 μm (preferably 0.05-3 μm).
5. The fiber of claim 1, wherein the multi-branched filler is substantially uniformly dispersed in the matrix, or, there is substantially no agglomerated structure of the multi-branched filler in the matrix, or, the minimum distance between any two adjacent multi-branched fillers in the matrix is greater than 0.1 μm (preferably greater than 5 μm).
6. The fiber of claim 1, wherein the multi-branched filler is selected from at least one of inorganic compound whiskers and organic compound whiskers, preferably selected from at least one of inorganic compound whiskers.
7. The fiber of claim 6, wherein the inorganic compound is at least one selected from inorganic oxygen-containing compounds, preferably at least one selected from metal oxides, metal hydroxides and metal oxyacid salts, in particular at least one selected from metal oxyacid salts, such as at least one selected from silicon carbide, silicon nitride, aluminum oxide, zinc oxide, magnesium oxide, calcium carbonate, basic magnesium sulfate, aluminum borate, magnesium borate, potassium titanate and calcium sulfate; or, the organic compound is at least one selected from organic polymers, preferably at least one selected from cellulose, polyester, polyamide and poly 4-hydroxybenzoate (PHB).
8. The fiber of claim 1, wherein the multi-branched filler has been subjected to surface chemical modification, such as surface chemical modification with a silane coupling agent.
9. The fiber of claim 8, wherein the silane coupling agent is selected from at least one of aminopropyltriethoxysilane, γ-(glycidyloxy)propyltrimethoxysilane, and γ-(methacryloyloxy)propyltrimethoxysilane.
10. The fiber of claim 1, wherein the multi-branched filler has been subjected to a surface physical modification treatment, such as a surface roughening treatment and / or a surface polymer coating treatment.
11. The fiber of claim 10, wherein the polymer is selected from at least one of thermoplastic polymers, thermosetting polymers and rubbers, preferably selected from at least one of cellulose esters, olefin polymers (polyvinyl acetate, polyvinyl alcohol, perchlorethylene, polyisobutylene, etc.), polyesters, polyethers, polyamides, polyacrylates, α-cyanoacrylates, polyvinyl acetals, ethylene-vinyl acetate copolymers and isocyanates.
12. The fiber of claim 1, wherein the angle between any two adjacent dendrites is greater than 5° (preferably 30°-90°).
13. A method for producing ultra-high molecular weight polyethylene fiber, comprising the following steps: 1) optionally subjecting a multi-branched filler (such as whiskers) to a surface chemical modification and / or surface physical modification to obtain a modified multi-branched filler, wherein the multi-branched filler has a plurality of (preferably at least 2, more preferably 2-10 or 3-8) dendrites in its structure, and the plurality of dendrites are identical or different to each other, and the length (calculated from the root) of each independently ranges from 5 to 2000 μm (preferably 10 to 300 μm), 2) mixing the modified multi-branched filler or the multi-branched filler, ultra-high molecular weight polyethylene and a solvent to obtain a spinning solution, 3) Spinning the spinning solution into the polyethylene fiber.
14. The manufacturing method according to claim 13, wherein before performing step 1), it further comprises a step of drying the multi-branched filler, wherein the drying comprises: Reduce pressure, the drying temperature is 80-200°C (preferably 90-120°C), and the drying time is 0.5-10h (preferably 1-4h).
15. The manufacturing method according to claim 13, wherein the surface chemical modification treatment comprises: A silane coupling agent is used, the amount of the silane coupling agent is 0.8-5wt% (preferably 1-3wt%) of the weight of the multi-branched filler, the treatment temperature is 40-100° C. (preferably 70-90° C.), and the treatment time is 1-120 min (preferably 5-30 min).
16. The manufacturing method according to claim 13, wherein the surface physical modification treatment comprises: The surface is coated with a polymer in an amount (dry basis) of at least 1%wt% (preferably 5-10wt%) of the multi-branched filler, at a treatment temperature of at least 30°C (preferably 40-60°C) and for at least 1 min (preferably 5-10 min).
17. The manufacturing method of claim 13, wherein in step 3), the spinning comprises: In the gel spinning method, the primary stretching ratio of the spinneret is 3-10, the super stretching temperature is 80-150°C, and the super stretching ratio is 6-20 (preferably 8-15).
18. A fabric comprising the ultra-high molecular weight polyethylene fiber of claim 1 or the ultra-high molecular weight polyethylene fiber manufactured by the manufacturing method of claim 13.
Citation Information
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