CN115923209A - Continuous fiber cloth/UHMWPE composite material and double-layer co-extrusion molding process thereof - Google Patents
Continuous fiber cloth/UHMWPE composite material and double-layer co-extrusion molding process thereof Download PDFInfo
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Abstract
Description
技术领域technical field
本发明涉及聚合物加工成型领域,具体涉及一种连续纤维布/UHMWPE复合材料及其双层共挤成型工艺。The invention relates to the field of polymer processing and molding, in particular to a continuous fiber cloth/UHMWPE composite material and a double-layer co-extrusion molding process thereof.
背景技术Background technique
超高分子量聚乙烯(UHMWPE)是粘均分子量大于150万的聚乙烯(PE),是一种新型热塑性工程塑料,由于其分子链长,分子量极高,优异的力学性能、耐冲击、耐磨损、自润滑性、耐化学腐蚀等性能。UHMWPE是目前已发现的耐磨性最好的塑料,所以其板材、管材、异型材广泛应用于石油化工、机械、纺织、造纸、矿业、粮食加工及体育运动器械等领域,其中以大型包装容器和管道的应用最为广泛。另外,基于UHMWPE优异的生理惰性,已作为心脏瓣膜、矫形外科零件、人工关节等在医药卫生领域使用。Ultra-high molecular weight polyethylene (UHMWPE) is polyethylene (PE) with a viscosity average molecular weight greater than 1.5 million. It is a new type of thermoplastic engineering plastic. Due to its long molecular chain and extremely high molecular weight, it has excellent mechanical properties, impact resistance, and wear resistance Loss, self-lubrication, chemical corrosion resistance and other properties. UHMWPE is the plastic with the best wear resistance that has been found so far, so its plates, pipes, and profiles are widely used in petrochemical, machinery, textile, paper, mining, grain processing, and sports equipment and other fields, among which large packaging containers And pipelines are the most widely used. In addition, based on the excellent physiological inertia of UHMWPE, it has been used in the field of medicine and health as heart valves, orthopedic parts, artificial joints, etc.
以UHMWPE为基础原料制造的制品工件,具有高强高抗冲性,即使在-40℃环境下仍保持优异的韧性和强度,但是UHMWPE有一个明显的缺陷,其耐高温性能差、耐磨却不耐刮擦。随着UHMWPE制品的广泛应用,其制品的形状、尺寸也呈现出多样性,对尺寸的精确度、产品的耐高温性、防切割性能要求也在不断的提高,尤其是一些异形件,例如导轨、滑块、齿轮等。但是由于本身的收缩率较高,约为2-3%,因此在成型过程中极易产生翘曲、椭圆、局部收缩不均等尺寸不稳定现象。The workpiece made of UHMWPE has high strength and high impact resistance, and it still maintains excellent toughness and strength even in the environment of -40°C. However, UHMWPE has an obvious defect, which is poor in high temperature resistance and wear resistance. Scratch resistant. With the wide application of UHMWPE products, the shape and size of the products are also diverse, and the requirements for dimensional accuracy, high temperature resistance and cutting resistance of the products are also constantly improving, especially for some special-shaped parts, such as guide rails , sliders, gears, etc. However, due to the high shrinkage rate of about 2-3%, it is easy to produce dimensional instability such as warping, ellipse, and local uneven shrinkage during the molding process.
发明内容Contents of the invention
本发明的目的就是为了克服上述现有技术存在的缺陷的至少一个而提供一种连续纤维布/UHMWPE复合材料及其双层共挤成型工艺。有效解决了现有UHMWPE制品尺寸精确度、耐温性、防切割性的问题,促进UHMWPE制品产业的发展。The object of the present invention is to provide a continuous fiber cloth/UHMWPE composite material and its double-layer co-extrusion molding process in order to overcome at least one of the above-mentioned defects in the prior art. It effectively solves the problems of dimensional accuracy, temperature resistance and cutting resistance of existing UHMWPE products, and promotes the development of UHMWPE product industry.
本发明的目的可以通过以下技术方案来实现:The purpose of the present invention can be achieved through the following technical solutions:
本发明利用纤维布/UHMWPE双层共挤成型工艺,根据制品的形状、厚度及应用需求,设计合适的模具,设计合理的温度分布,形成阶梯式温度分布,达到精确调整制品尺寸,并选取合适的纤维布,达到防切割和提高UHMWPE制品耐温性,具体方案如下:The present invention uses the fiber cloth/UHMWPE double-layer co-extrusion molding process to design a suitable mold according to the shape, thickness and application requirements of the product, design a reasonable temperature distribution, and form a stepped temperature distribution to accurately adjust the size of the product and select a suitable fiber cloth to achieve anti-cutting and improve the temperature resistance of UHMWPE products, the specific plan is as follows:
一种连续纤维布/UHMWPE复合材料的双层共挤成型工艺,该工艺包括以下步骤:A double-layer co-extrusion molding process of continuous fiber cloth/UHMWPE composite material, the process comprises the following steps:
将超高分子量聚乙烯基体材料通过单螺杆挤出机挤出,在螺杆挤出机进料段,将超高分子量聚乙烯材料加热到熔融温度以上,然后熔体被输送进入模具成型段,在模具成型段内经过熔压-压缩成型,制备成熔体型胚;成型方法包括挤出成型、注塑成型、模压成型;The ultra-high molecular weight polyethylene matrix material is extruded through a single-screw extruder. In the feeding section of the screw extruder, the ultra-high molecular weight polyethylene material is heated above the melting temperature, and then the melt is transported into the mold forming section. Melt-compression molding is carried out in the molding section of the mold to prepare a melt parison; molding methods include extrusion molding, injection molding, and compression molding;
先将纤维布表面两侧分别预先贴合薄膜,再将该纤维布通过预复合加热辊穿过特定型腔1,在冷却段之前与熔体型胚形成复合共挤,形成连续纤维布/UHMWPE复合材料,再通过特定型腔2冷却定型,通过牵引机牵出。Firstly, the two sides of the surface of the fiber cloth are pre-laminated with films, and then the fiber cloth is passed through the specific cavity 1 through the pre-compound heating roller, and the composite co-extrusion is formed with the melt parison before the cooling section to form a continuous fiber cloth/UHMWPE The composite material is then cooled and shaped through a specific cavity 2, and pulled out by a tractor.
进一步地,所述的纤维布为超高分子量聚乙烯纤维与耐温纤维混纺所制备的纤维布。其他纤维混纺主要是为了改善超高分子量聚乙烯纤维不耐高温的缺点,一般超高分子量聚乙烯纤维耐温性120-140℃,但是芳纶、碳纤维、玻璃纤维等耐温性都在200℃以上。超高分子量聚乙烯纤维具有高强高模,优异的耐磨性及防切割性能,混纺后能提高使用温度,又突出优异的耐磨和防切割性能。Further, the fiber cloth is a fiber cloth prepared by blending ultra-high molecular weight polyethylene fibers and heat-resistant fibers. Other fiber blending is mainly to improve the shortcoming of ultra-high molecular weight polyethylene fiber that is not resistant to high temperature. Generally, the temperature resistance of ultra-high molecular weight polyethylene fiber is 120-140°C, but the temperature resistance of aramid fiber, carbon fiber, glass fiber, etc. is all at 200°C. above. Ultra-high molecular weight polyethylene fiber has high strength and high modulus, excellent wear resistance and cut resistance. After blending, it can increase the use temperature and highlight excellent wear resistance and cut resistance.
进一步地,所述的超高分子量聚乙烯纤维与耐温纤维占据纤维布的面积之比为(2-5):1,所述纤维布的面密度60-200g/m2,混纺采用平纹或斜纹方式编织。Further, the ratio of the area of the fiber cloth occupied by the ultra-high molecular weight polyethylene fiber to the temperature-resistant fiber is (2-5):1, the surface density of the fiber cloth is 60-200g/m 2 , and the blending adopts plain weave or Twill weave.
进一步地,所述耐温纤维为耐温性不低于200℃的纤维,包括丙纶纤维、尼龙纤维、芳纶纤维、碳纤维、玻璃纤维、涤纶纤维、粘胶纤维或腈纶纤维中的一种或者几种;所述超高分子量聚乙烯纤维强度25-40cN/dtex,细度50-1600D,优选地,纤维强度30-35cN/dtex,细度为500-1000D。Further, the temperature-resistant fiber is a fiber with a temperature resistance not lower than 200°C, including one of polypropylene fiber, nylon fiber, aramid fiber, carbon fiber, glass fiber, polyester fiber, viscose fiber or acrylic fiber or Several types; the ultra-high molecular weight polyethylene fiber has a strength of 25-40cN/dtex and a fineness of 50-1600D, preferably, a fiber strength of 30-35cN/dtex and a fineness of 500-1000D.
进一步地,所述超高分子量聚乙烯的分子量为100万-600万。Further, the molecular weight of the ultra-high molecular weight polyethylene is 1 million to 6 million.
进一步地,所述的具体步骤为:Further, the specific steps described are:
(1)将超高分子量聚乙烯基体材料通过单螺杆挤出机挤出,在螺杆挤出机进料段,将超高分子量聚乙烯材料加热到熔融温度以上,然后熔体被输送进入模具成型段,在模具成型段内经过熔压-压缩,制备成熔体型胚;(1) Extrude the ultra-high molecular weight polyethylene base material through a single-screw extruder. In the feeding section of the screw extruder, the ultra-high molecular weight polyethylene material is heated above the melting temperature, and then the melt is transported into the mold for molding section, which is melt-compressed in the mold forming section to prepare a melt parison;
(2)先将纤维布表面两侧分别预先贴合薄膜,再将该纤维布通过预复合加热辊穿过特定型腔1,在冷却段之前与熔体型胚形成复合共挤,形成连续纤维布/UHMWPE复合材料,再通过特定型腔2冷却定型,通过牵引机牵出。(2) Pre-laminate the film on both sides of the surface of the fiber cloth, and then pass the fiber cloth through the specific cavity 1 through the pre-composite heating roller, and form a composite co-extrusion with the melt parison before the cooling section to form a continuous fiber The cloth/UHMWPE composite material is cooled and shaped through a specific cavity 2, and pulled out by a tractor.
进一步地,步骤(1)中,单螺杆的挤出温度控制为150-280℃逐步升温;模具成型段内依次设有分流段、压缩段和定型段,温度控制为250-180℃阶梯式逐步降温,其中分流段235-280℃、压缩段200-235℃、定型段150-200℃。Further, in step (1), the single-screw extrusion temperature is controlled to be 150-280°C and the temperature is gradually raised; the mold forming section is sequentially provided with a split section, a compression section and a shaping section, and the temperature is controlled to be 250-180°C in a stepwise manner. Cool down, where the diversion section is 235-280°C, the compression section is 200-235°C, and the shaping section is 150-200°C.
进一步地,步骤(2)中,特定型腔具有内外测多点位阶段式控温效果,型腔内侧温度控制为150-180℃,外侧温度控制为135-160℃;复合共挤的温度为150-180℃,复合段的压缩比为(1.1-1.8):1,特定型腔1模板压力通过压力传感器自动调整可控。Further, in step (2), the specific cavity has a multi-point staged temperature control effect of internal and external measurements. The temperature inside the cavity is controlled at 150-180°C, and the temperature at the outside is controlled at 135-160°C; the temperature of the composite co-extrusion is 150-180°C, the compression ratio of the composite section is (1.1-1.8):1, and the specific cavity 1 template pressure is automatically adjusted and controlled by the pressure sensor.
进一步地,所述的薄膜包括超高分子量聚乙烯薄膜和EVA薄膜,贴合时,形成超高分子量聚乙烯薄膜/EVA薄膜/纤维布/EVA薄膜的四层复合纤维布,UHMWPE薄膜位于型腔外侧,厚度为0.2-1mm,EVA薄膜的厚度为0.2-0.5mm。Further, the film includes an ultra-high molecular weight polyethylene film and an EVA film. When laminating, a four-layer composite fiber cloth of ultra-high molecular weight polyethylene film/EVA film/fiber cloth/EVA film is formed, and the UHMWPE film is located in the cavity Outside, the thickness is 0.2-1mm, and the thickness of EVA film is 0.2-0.5mm.
一种如上所述双层共挤成型工艺制备的连续纤维布/UHMWPE复合材料。A continuous fiber cloth/UHMWPE composite material prepared by the above-mentioned double-layer co-extrusion molding process.
与现有技术相比,本发明具有以下优点:Compared with the prior art, the present invention has the following advantages:
(1)本发明设计合理的温度分布,形成阶梯式温度分布,利用模温机、冷水机等相关控温设备,精确调节温差,控制材料降温速率及收缩速度,进而达到精确调整制品尺寸目的;(1) The present invention designs a reasonable temperature distribution to form a stepped temperature distribution, and uses related temperature control equipment such as a mold temperature machine and a water chiller to accurately adjust the temperature difference, control the cooling rate and shrinkage rate of the material, and then achieve the purpose of accurately adjusting the size of the product;
(2)本发明利用超高分子量聚乙烯纤维与其他纤维混纺,兼具超高分子量聚乙烯纤维的高强高模,优异的防切割性能,芳纶纤维、碳纤维等纤维的优异耐温性,复合在超高分子量聚乙烯制品表面,从而改善了超高分子量聚乙烯耐磨不耐刮擦,耐低温不耐高温的缺陷,进而拓展了制品的使用寿命和使用范围;(2) The present invention utilizes the blending of ultra-high molecular weight polyethylene fiber and other fibers, which has the high strength and high modulus of ultra-high molecular weight polyethylene fiber, excellent cutting resistance performance, excellent temperature resistance of fibers such as aramid fiber and carbon fiber, and composite On the surface of ultra-high-molecular-weight polyethylene products, the defects of ultra-high-molecular-weight polyethylene, such as wear resistance and scratch resistance, low temperature resistance and high temperature resistance, are improved, thereby extending the service life and scope of use of the product;
(3)本发明的特定型腔具有挤压定型,调整收缩率等作用。型腔内腔形状是跟前面模头出来一样的,随制品形状来的。一般来说,现在成型的型腔,大多都是冷却定型,很少做到可控,以及复合过程中两种或者几种材料复合收缩率可控调整的。本发明的特定型腔是通过压力传感器、高低温模温机来做到复合过程中两种或者几种材料复合收缩率可控调整的。(3) The specific cavity of the present invention has functions such as extruding and shaping, adjusting shrinkage rate, and the like. The shape of the inner cavity of the cavity is the same as that of the previous die head, and it comes with the shape of the product. Generally speaking, most of the molded cavities are cooled and shaped, and they are rarely controllable, and the composite shrinkage rate of two or several materials can be controlled and adjusted during the composite process. The specific mold cavity of the present invention can controllably adjust the composite shrinkage rate of two or several materials in the composite process through a pressure sensor and a high and low temperature mold temperature controller.
附图说明Description of drawings
图1为本发明挤出复合成型示意图。Fig. 1 is a schematic diagram of extrusion composite molding of the present invention.
具体实施方式Detailed ways
下面结合附图和具体实施例对本发明进行详细说明。本实施例在以本发明技术方案为前提下进行实施,给出了详细的实施方式和具体的操作过程,但本发明的保护范围不限于下述的实施例。The present invention will be described in detail below in conjunction with the accompanying drawings and specific embodiments. This embodiment is carried out on the premise of the technical solution of the present invention, and the detailed implementation and specific operation process are given, but the protection scope of the present invention is not limited to the following embodiments.
一种连续纤维布/UHMWPE复合材料及其双层共挤成型工艺,包括以下步骤:A continuous fiber cloth/UHMWPE composite material and a double-layer co-extrusion molding process thereof, comprising the following steps:
(1)超高分子量聚乙烯材料通过单螺杆挤出机挤出,在螺杆挤出机进料段,将超高分子量聚乙烯材料加热到熔融温度以上,然后熔体被输送进入模具成型段,在模具成型段内经过熔压-压缩制备成熔体型胚;超高分子量聚乙烯纤维强度25-40cN/dtex,细度50-1600D,优选为纤维强度30-35cN/dtex,细度为500-1000D。基体为超高分子量聚乙烯粉体,分子量为100万-600万。单螺杆的挤出温度控制为150-280℃逐步升温;模具成型段内依次设有分流段、压缩段和定型段,其温度控制为250-180℃阶梯式逐步降温,其中分流段235-280℃、压缩段200-235℃、定型段150-200℃。(1) The ultra-high molecular weight polyethylene material is extruded through a single-screw extruder. In the feeding section of the screw extruder, the ultra-high molecular weight polyethylene material is heated above the melting temperature, and then the melt is transported into the mold forming section. In the molding section of the mold, it is melt-compressed to prepare a melt parison; the ultra-high molecular weight polyethylene fiber strength is 25-40cN/dtex, and the fineness is 50-1600D, preferably the fiber strength is 30-35cN/dtex, and the fineness is 500 -1000D. The matrix is ultra-high molecular weight polyethylene powder with a molecular weight of 1 million to 6 million. The single-screw extrusion temperature control is 150-280°C and the temperature is gradually raised; the mold forming section is equipped with a split section, a compression section and a shaping section in sequence, and its temperature control is 250-180°C. ℃, compression section 200-235℃, setting section 150-200℃.
(2)纤维布表面两侧预先复合超高分子量聚乙烯/EVA薄膜,形成超高分子量聚乙烯薄膜/EVA薄膜/纤维布/EVA薄膜的四层复合纤维布,再将该纤维布通过特定型腔穿过模具,在冷却段之前与熔体型胚形成复合共挤,复合温度150-180℃,复合段的压缩比(1.1-1.8):1,从而形成共挤制品。纤维布为超高分子量聚乙烯纤维与其他纤维的一种或几种混纺所制备的纤维布。其他纤维包括丙纶纤维、尼龙纤维、芳纶纤维、碳纤维、玻璃纤维、涤纶纤维、粘胶纤维、腈纶纤维中的一种或者几种。将超高分子量聚乙烯纤维与其他纤维采用平纹或斜纹方式编织。超高分子量聚乙烯纤维与其他纤维面积比例为(2-5):1,纤维布的面密度60-200g/m2。特定型腔具有内外测多点位阶段式控温效果,型腔内侧温度控制为150-180℃,外侧温度控制为135-160℃。(2) Both sides of the surface of the fiber cloth are pre-composited with ultra-high molecular weight polyethylene/EVA film to form a four-layer composite fiber cloth of ultra-high molecular weight polyethylene film/EVA film/fiber cloth/EVA film, and then pass the fiber cloth through a specific type The cavity passes through the mold, and forms a composite co-extrusion with the melt parison before the cooling section. The composite temperature is 150-180°C, and the compression ratio of the composite section (1.1-1.8): 1, thereby forming a co-extruded product. Fiber cloth is a fiber cloth prepared by one or several blends of ultra-high molecular weight polyethylene fibers and other fibers. Other fibers include one or more of polypropylene fibers, nylon fibers, aramid fibers, carbon fibers, glass fibers, polyester fibers, viscose fibers, and acrylic fibers. Weave UHMWPE fiber with other fibers in plain weave or twill weave. The area ratio of UHMWPE fiber to other fibers is (2-5):1, and the surface density of the fiber cloth is 60-200g/m 2 . The specific cavity has a multi-point staged temperature control effect of internal and external measurements. The temperature inside the cavity is controlled at 150-180°C, and the temperature at the outside is controlled at 135-160°C.
实施例1Example 1
一种连续纤维布/UHMWPE复合材料及其双层共挤成型工艺,挤出成型超高分子量聚乙烯异型材,原材料分子量200万,首先将超高分子量聚乙烯材料加热到熔融温度以上的温度,熔体在经过模具的压缩段被挤压为高压熔体,将超高分子量聚乙烯纤维与芳纶纤维按照面积比2:1混纺制成的纤维布,纤维布面密度60g/m2,表面两侧复合超高分子量聚乙烯薄膜/EVA薄膜,外侧超高分子量聚乙烯薄膜厚度1mm,内侧EVA薄膜厚度为0.2mm,然后再与该高压熔体在定型段进行复合,复合温度180℃,复合段压缩比1.5:1,再经过冷却成型成为制品。模具成型段分为分流段、压缩段、定型段,加热温度的范围分别为250℃、210℃、180℃。型腔内侧控制温度160℃,型腔外侧控制温度150℃。挤出制品力学性能见附表1。A continuous fiber cloth/UHMWPE composite material and its double-layer co-extrusion molding process, extruding ultra-high molecular weight polyethylene profiles, raw material molecular weight 2 million, first heating the ultra-high molecular weight polyethylene material to a temperature above the melting temperature, The melt is extruded into a high-pressure melt through the compression section of the mold, and the fiber cloth made by blending ultra-high molecular weight polyethylene fiber and aramid fiber according to the area ratio of 2:1, the surface density of the fiber cloth is 60g/m 2 , the surface Composite ultra-high molecular weight polyethylene film/EVA film on both sides, the thickness of the outer ultra-high molecular weight polyethylene film is 1mm, and the thickness of the inner EVA film is 0.2mm, and then compound with the high-pressure melt in the shaping section, the compounding temperature is 180 ℃, compounding The compression ratio of the stage is 1.5:1, and then it is cooled and formed into a finished product. The molding section of the mold is divided into a split section, a compression section, and a shaping section, and the heating temperature ranges are 250°C, 210°C, and 180°C. The temperature inside the cavity is controlled at 160°C, and the temperature outside the cavity is controlled at 150°C. The mechanical properties of extruded products are shown in attached table 1.
实施例2Example 2
一种连续纤维布/UHMWPE复合材料及其双层共挤成型工艺,挤出成型超高分子量聚乙烯异型材,原材料分子量350万,首先将超高分子量聚乙烯材料加热到熔融温度以上的温度,熔体在经过模具的压缩段被挤压为高压熔体,将超高分子量聚乙烯纤维与尼龙纤维按照面积比5:1混纺制成的纤维布,纤维布面密度90g/m2,表面两侧复合超高分子量聚乙烯薄膜/EVA薄膜,外侧超高分子量聚乙烯薄膜厚度0.3mm,内侧EVA薄膜厚度为0.5mm,然后再与该高压熔体在定型段进行复合,复合温度150℃,复合段压缩比1.2:1,再经过冷却成型成为制品。模具成型段分为分流段、压缩段、定型段,加热温度的范围分别为225℃、200℃、150℃。型腔内侧控制温度150℃,型腔外侧控制温度135℃。挤出制品力学性能见附表1。A continuous fiber cloth/UHMWPE composite material and its double-layer co-extrusion molding process, extruding ultra-high molecular weight polyethylene profiles, the molecular weight of raw materials is 3.5 million, first heating the ultra-high molecular weight polyethylene material to a temperature above the melting temperature, The melt is extruded into a high-pressure melt through the compression section of the mold, and the fiber cloth is made by blending ultra-high molecular weight polyethylene fiber and nylon fiber according to the area ratio of 5:1. The surface density of the fiber cloth is 90g/m 2 , and the surface is double Composite ultra-high molecular weight polyethylene film/EVA film on the side, the thickness of the outer ultra-high molecular weight polyethylene film is 0.3mm, and the thickness of the inner EVA film is 0.5mm, and then compound with the high-pressure melt in the shaping section, the compounding temperature is 150 ℃, compounding The compression ratio of the stage is 1.2:1, and then it is cooled and formed into a product. The molding section of the mold is divided into a split section, a compression section, and a shaping section, and the heating temperature ranges are 225°C, 200°C, and 150°C. The temperature inside the cavity is controlled at 150°C, and the temperature outside the cavity is controlled at 135°C. The mechanical properties of extruded products are shown in attached table 1.
实施例3Example 3
一种连续纤维布/UHMWPE复合材料及其双层共挤成型工艺,挤出成型超高分子量聚乙烯片材,原材料分子量450万,首先将超高分子量聚乙烯材料加热到熔融温度以上的温度,熔体在经过模具的压缩段被挤压为高压熔体,将超高分子量聚乙烯纤维与碳纤维按照面积比3:1混纺制成的纤维布,纤维布面密度150g/m2,表面两侧复合超高分子量聚乙烯薄膜/EVA薄膜,外侧超高分子量聚乙烯薄膜厚度0.5mm,内侧EVA薄膜厚度为0.3mm,然后再与该高压熔体在定型段进行复合,复合温度175℃,复合段压缩比1.3:1,再经过冷却成型成为制品。模具成型段分为分流段、压缩段、定型段,加热温度的范围分别为235℃、210℃、160℃。型腔内侧控制温度180℃,型腔外侧控制温度160℃。挤出制品力学性能见附表1。A continuous fiber cloth/UHMWPE composite material and its double-layer co-extrusion molding process, extruded ultra-high molecular weight polyethylene sheet material, the molecular weight of the raw material is 4.5 million, first the ultra-high molecular weight polyethylene material is heated to a temperature above the melting temperature, The melt is extruded into a high-pressure melt in the compression section of the mold, and the fiber cloth is made by blending ultra-high molecular weight polyethylene fibers and carbon fibers according to the area ratio of 3:1. The surface density of the fiber cloth is 150g/m 2 . Composite ultra-high molecular weight polyethylene film/EVA film, the thickness of the outer ultra-high molecular weight polyethylene film is 0.5mm, and the thickness of the inner EVA film is 0.3mm, and then compound with the high-pressure melt in the shaping section, the compounding temperature is 175°C, the compounding stage The compression ratio is 1.3:1, and then cooled and formed into products. The molding section of the mold is divided into a split section, a compression section, and a shaping section, and the heating temperature ranges are 235°C, 210°C, and 160°C. The temperature inside the cavity is controlled at 180°C, and the temperature outside the cavity is controlled at 160°C. The mechanical properties of extruded products are shown in attached table 1.
表1实施例1-3制品力学性能Table 1 Example 1-3 product mechanical properties
*注:滑动摩擦系数测试采取往复式,测试条件为压力5N,频率为1Hz。*Note: The sliding friction coefficient test adopts reciprocating type, the test condition is pressure 5N, frequency 1Hz.
对比例1Comparative example 1
一种成型工艺,挤出成型超高分子量聚乙烯异型材,原材料分子量200万,首先将超高分子量聚乙烯材料加热到熔融温度以上的温度,熔体在经过模具的压缩段被挤压为高压熔体,此后高压熔体经过冷却段直接冷却成型为制品。模具成型段分为分流段、压缩段、定型段,加热温度的范围分别为250℃、210℃、180℃。A molding process, extruding ultra-high molecular weight polyethylene profiles, the molecular weight of the raw material is 2 million, first heating the ultra-high molecular weight polyethylene material to a temperature above the melting temperature, and the melt is extruded to a high pressure in the compression section of the mold After that, the high-pressure melt is directly cooled and formed into products through the cooling section. The molding section of the mold is divided into a split section, a compression section, and a shaping section, and the heating temperature ranges are 250°C, 210°C, and 180°C.
对比例2Comparative example 2
一种成型工艺,挤出成型超高分子量聚乙烯片材,原材料分子量300万,首先将超高分子量聚乙烯材料加热到熔融温度以上的温度,熔体在经过模具的压缩段被挤压为高压熔体,此后高压熔体经过冷却段直接冷却成型成为制品。模具成型段分为分流段、压缩段、定型段,加热温度的范围分别为235℃、210℃、160℃。A molding process, extruding ultra-high molecular weight polyethylene sheets, the molecular weight of the raw material is 3 million, first heating the ultra-high molecular weight polyethylene material to a temperature above the melting temperature, and the melt is extruded to a high pressure in the compression section of the mold After that, the high-pressure melt is directly cooled and formed into a product through the cooling section. The molding section of the mold is divided into a split section, a compression section, and a shaping section, and the heating temperature ranges are 235°C, 210°C, and 160°C.
对比例3Comparative example 3
一种成型工艺,挤出成型超高分子量聚乙烯异型材,原材料分子量200万,首先将超高分子量聚乙烯材料加热到熔融温度以上的温度,熔体在经过模具的压缩段被挤压为高压熔体,将超高分子量聚乙烯纤维与芳纶纤维按照面积比2:1混纺制成的纤维布,纤维布面密度60g/m2,表面内侧EVA薄膜厚度为0.2mm,然后再与该高压熔体在定型段进行复合,复合温度180℃,复合段压缩比1.5:1,此后再经过冷却段直接冷却成型为制品。模具成型段分为分流段、压缩段、定型段,加热温度的范围分别为250℃、210℃、180℃。型腔内侧控制温度160℃,型腔外侧控制温度150℃。A molding process, extruding ultra-high molecular weight polyethylene profiles, the molecular weight of the raw material is 2 million, first heating the ultra-high molecular weight polyethylene material to a temperature above the melting temperature, and the melt is extruded to a high pressure in the compression section of the mold Melt, the fiber cloth made by blending ultra-high molecular weight polyethylene fiber and aramid fiber according to the area ratio of 2:1, the fiber cloth surface density is 60g/m 2 , the thickness of the inner EVA film on the surface is 0.2mm, and then combined with the high pressure The melt is compounded in the shaping section, the compounding temperature is 180°C, the compression ratio of the compounding section is 1.5:1, and then it is directly cooled and formed into a product through the cooling section. The molding section of the mold is divided into a split section, a compression section, and a shaping section, and the heating temperature ranges are 250°C, 210°C, and 180°C. The temperature inside the cavity is controlled at 160°C, and the temperature outside the cavity is controlled at 150°C.
表2对比例1-3制品力学性能Table 2 Comparative Examples 1-3 product mechanical properties
*注:滑动摩擦系数测试采取往复式,测试条件为压力5N,频率为1Hz。*Note: The sliding friction coefficient test adopts reciprocating type, the test condition is pressure 5N, frequency 1Hz.
翘曲度数据,从侧面印证尺寸精确度调节有成效。超高分子量聚乙烯片材和超高分子量聚乙烯纤维同是用超高分子量聚乙烯树脂加工而成,本发明中片材是通过挤出成型工艺成型,相关的物性参数可参考表2。超高分子量聚乙烯的熔体粘度很高,流动性很差,粘结性不好,如不在纤维上复合薄膜,很难单纯的通过共挤将纤维布和超高分子量聚乙烯基体复合在一起。纤维布外侧不复合一层超高分子量聚乙烯薄膜,可以体现在摩擦系数上会不一样。The warpage data proves from the side that the dimensional accuracy adjustment is effective. The ultra-high molecular weight polyethylene sheet and the ultra-high molecular weight polyethylene fiber are both processed with ultra-high molecular weight polyethylene resin. In the present invention, the sheet is formed by an extrusion molding process. The relevant physical parameters can refer to Table 2. UHMWPE has a high melt viscosity, poor fluidity, and poor cohesiveness. If the film is not compounded on the fiber, it is difficult to simply combine the fiber cloth and the UHMWPE matrix through co-extrusion. . The outside of the fiber cloth is not compounded with a layer of ultra-high molecular weight polyethylene film, which can be reflected in the friction coefficient will be different.
以上所述,仅是本发明的较佳实施例而已,并非是对本发明作其它形式的限制,任何熟悉本专业的技术人员可能利用上述揭示的技术内容加以变更或改型为等同变化的等效实施例。但是凡是未脱离本发明技术方案内容,依据本发明的技术实质对以上实施例所作的任何简单修改、等同变化与改型,仍属于本发明技术方案的保护范围。The above is only a preferred embodiment of the present invention, and is not intended to limit the present invention to other forms. Any skilled person who is familiar with this profession may use the technical content disclosed above to change or remodel it into an equivalent change. Example. However, any simple modifications, equivalent changes and modifications made to the above embodiments according to the technical essence of the present invention without departing from the content of the technical solution of the present invention still belong to the protection scope of the technical solution of the present invention.
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