CN109456458A - 用于鞋材的聚醚酯型tpu及其制备方法 - Google Patents

用于鞋材的聚醚酯型tpu及其制备方法 Download PDF

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CN109456458A
CN109456458A CN201811140101.3A CN201811140101A CN109456458A CN 109456458 A CN109456458 A CN 109456458A CN 201811140101 A CN201811140101 A CN 201811140101A CN 109456458 A CN109456458 A CN 109456458A
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polyether ester
footwear material
type tpu
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代金辉
徐艳艳
宋小娜
罗杰
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Shandong Inov Polyurethane Co Ltd
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Abstract

本发明属于高分子材料技术领域,具体涉及一种用于鞋材的聚醚酯型TPU及其制备方法。所述的用于鞋材的聚醚酯型TPU,由下列质量份数的物质组成:二异氰酸酯20‑40份;聚醚酯多元醇50‑70份;羟基硅油3‑8份;碳纳米管0.002‑0.02份;扩链剂5‑10份;催化剂0.5‑1份。制得的聚醚酯型TPU不仅具有优良的耐水解和低温柔顺性,同时还具有力学性能优异和耐热耐油的特性。本发明提供的制备方法,科学合理,简单易行。

Description

用于鞋材的聚醚酯型TPU及其制备方法
技术领域
本发明属于高分子材料技术领域,具体涉及一种用于鞋材的聚醚酯型TPU及其制备方法。
背景技术
热塑性聚氨酯弹性体(TPU)是一种性能优良的高分子合成材料,既具有橡胶的弹性又有塑料的硬度,而且还具有良好的机械性能、耐磨性和回弹性能,使其广泛应用于各个工业领域。TPU的软质段可使用多种的聚醇,大致上可分为聚醚系及聚酯系两种。目前许多商品热塑性聚氨酯都是聚酯型的,这种热塑性聚氨酯的耐磨性、抗撕裂性以及拉伸和撕裂强度都优于聚醚型热塑性聚氨酯,聚酯型热塑性聚氨酯在油、脂和水中的溶胀性也比较小。但其在耐水解性、耐微生物降解性和低温性、柔顺性等方面却不具备聚醚型聚氨酯弹性体的优势。TPU鞋材产品具有轻便、弹性好、易加工和可回收等优点,是TPU市场中不可或缺的组成部分,鞋材产品尤其是高端鞋材产品要求产品在拥有良好力学性能的同时必须保持优良的耐水解及耐低温性能。如何克服两者的缺点,实现优势互补成近年来人们关注的热点。
Pxominska等将聚醚与聚酯两种多元醇物理混合后合成弹性体,具有较为优良的综合性能。然而聚酯多元醇粘度较高,物理混合时操作不便,且聚醚、聚酯两种多元醇的相容性差,往往使制得的弹性体性能达不到预期效果。
发明内容
针对现有技术的不足,本发明的目的是提供一种用于鞋材的聚醚酯型TPU,不仅具有优良的耐水解和低温柔顺性,同时还具有力学性能优异和耐热耐油的特性。
同时,本发明还提供其制备方法,科学合理,简单易行。
本发明所述的用于鞋材的聚醚酯型TPU,由下列质量份数的物质组成:
二异氰酸酯为二苯基甲烷二异氰酸酯、氢化苯基甲烷二异氰酸酯或六亚甲基二异氰酸酯中一种或几种。
所述的聚醚酯多元醇的分子量为1000-2000,酯基与醚基的摩尔比为0.8-1.2。
优选的,所述的聚醚酯多元醇的分子量为2000,酯基与醚基的摩尔比为1。
所述的聚醚酯多元醇为聚四氢呋喃二醇/聚己二酸乙二醇酯二醇聚醚酯多元醇、聚氧化丙烯二醇/聚己二酸乙二醇酯二醇聚醚酯多元醇或聚乙二醇/聚己二酸乙二醇酯二醇聚醚酯多元醇中一种或几种。
所述的羟基硅油在25℃下粘度为500-5000cps。
所述的碳纳米管直径为50-200nm,长径比为100-500。
所述的扩链剂为1,4-丁二醇、1,6-己二醇、二羟甲基丙酸或二氯二氨基二苯甲烷中的一种或几种。
所述的催化剂为二月桂酸二丁基锡或辛酸亚锡中的一种或两种。
本发明所述的用于鞋材的聚醚酯型TPU的制备方法,包括以下步骤:
1)将质量比例的二异氰酸酯加入到A储料罐中,将质量比例的聚醚酯多元醇和羟基硅油加入到B储料罐中,将质量比例的扩链剂和催化剂加入到C储料罐中,在搅拌条件下,真空脱水,抽注到双螺杆挤出机中;
2)在双螺杆挤出机加料口加入质量比例的碳纳米管,110℃-190℃下,在双螺杆挤出机中反应,造粒得到TPU颗粒。
所述的步骤1中,真空脱水温度为90-120℃;搅拌速率为400-800r/min。
所述的步骤2中,双螺杆挤出机的喂料段温度为110-120℃,混合段温度为130-150℃,挤出段温度为170-180℃,机头温度为150-160℃。
与现有技术相比,本发明具有如下有益效果:
1.采用聚醚酯多元醇合成TPU提高了TPU的综合性能,其拉伸强度与相同硬度的聚醚型TPU相比提高了29%;经耐水解测试四周后其力学性能保持率可达到50%以上;
2.引入羟基硅油和碳纳米管赋予TPU更好的耐磨和机械强度,制得聚醚酯型TPU的DIN磨耗较之聚醚型TPU也降低了29%。
具体实施方式
下面结合实施例对本发明做进一步的说明。
实施例1
一种用于鞋材的聚醚酯型TPU,由包括以下质量份数的原料组成:
多元醇为聚四氢呋喃二醇/聚己二酸乙二醇酯二醇聚醚酯多元醇(PTMG/PEGA);羟基硅油在25℃下的粘度为500cp;碳纳米管的直径为100nm,长径比为500;
制备方法包括以下步骤:
1.将二异氰酸酯加入到A储料罐中,将多元醇和羟基硅油加入到B储料罐中,扩链剂和催化剂加入到C储料罐中,在500r/min速率下搅拌,110℃真空脱水,抽注到双螺杆挤出机中;
2.在双螺杆挤出机加料口加入碳纳米管,在120℃下,双螺杆挤出机中反应,造粒得到TPU颗粒;其中双螺杆挤出机的喂料段温度为110℃,混合段温度为130℃,挤出段温度为170℃,机头温度为150℃。
实施例2
一种用于鞋材的聚醚酯型TPU,由以下质量份数的原料组成:
多元醇为聚氧化丙烯二醇/聚己二酸乙二醇酯二醇聚醚酯多元醇;羟基硅油在25℃下的粘度为500cp;碳纳米管的直径为90nm,长径比为400。
制备方法包括以下步骤:
1.将二异氰酸酯加入到A储料罐中,将多元醇和羟基硅油加入到B储料罐中,扩链剂和催化剂加入到C储料罐中,在400r/min速率下搅拌,110℃真空脱水,抽注到双螺杆挤出机中;
2.在双螺杆挤出机加料口加入碳纳米管,在130℃下,双螺杆挤出机中反应,造粒得到TPU颗粒;其中双螺杆挤出机的喂料段温度为120℃,混合段温度为150℃,挤出段温度为180℃,机头温度为160℃。
实施例3
一种用于鞋材的聚醚酯型TPU,由以下质量份数的原料组成:
多元醇为聚四氢呋喃二醇/聚己二酸乙二醇酯二醇聚醚酯多元醇(PTMG/PEGA)和聚氧化丙烯二醇/聚己二酸乙二醇酯二醇聚醚酯多元醇(PPG/PEGA);羟基硅油在25℃下的粘度为5000cps;碳纳米管的直径为150nm,长径比为200。
制备方法包括以下步骤:
1.将二异氰酸酯加入到A储料罐中,多元醇、羟基硅油加入到B储料罐中,扩链剂和催化剂加入到C储料罐中,在400-800r/min速率下搅拌,110℃真空脱水,抽注到双螺杆挤出机中;
2.在双螺杆挤出机加料口加入碳纳米管,在110℃-190℃下,双螺杆挤出机中反应,造粒得到TPU颗粒;其中双螺杆挤出机的喂料段温度为110-120℃,混合段温度为130-150℃,挤出段温度为170-180℃,机头温度为150-160℃。
实施例4
一种用于鞋材的聚醚酯型TPU,由以下质量份数的原料组成:
多元醇为聚氧化丙烯二醇/聚己二酸乙二醇酯二醇聚醚酯多元醇(PPG/PEGA);羟基硅油在25℃下的粘度为800cp;碳纳米管的直径为50nm,长径比为100。
制备方法包括以下步骤:
1.将二异氰酸酯加入到A储料罐中,多元醇、羟基硅油加入到B储料罐中,扩链剂和催化剂加入到C储料罐中,在400-800r/min速率下搅拌,110℃真空脱水,抽注到双螺杆挤出机中;
2.在双螺杆挤出机加料口加入碳纳米管,在110℃-190℃下,双螺杆挤出机中反应,造粒得到TPU颗粒;其中双螺杆挤出机的喂料段温度为110-120℃,混合段温度为130-150℃,挤出段温度为170-180℃,机头温度为150-160℃。
实施例5
一种用于鞋材的聚醚酯型TPU,由以下质量份数的原料组成:
多元醇为聚乙二醇/聚己二酸乙二醇酯二醇聚醚酯多元醇(PEG/PEGA);羟基硅油在25℃下的粘度为1000cp;碳纳米管的直径为200nm,长径比为500。
用于鞋材的聚醚酯型TPU的制备方法包括以下步骤:
1.将二异氰酸酯加入到A储料罐中,多元醇、羟基硅油加入到B储料罐中,扩链剂和催化剂加入到C储料罐中,在400-800r/min速率下搅拌,110℃真空脱水,抽注到双螺杆挤出机中;2.在双螺杆挤出机加料口加入碳纳米管,在110℃-190℃下,双螺杆挤出机中反应,造粒得到TPU颗粒。其中双螺杆挤出机的喂料段温度为110-120℃,混合段温度为130-150℃,挤出段温度为170-180℃,机头温度为150-160℃。
对比例1
一种用于鞋材的聚醚酯型TPU,由包括以下质量份数的原料组成:
其中多元醇为聚己二酸乙二醇酯二醇多元醇(PEGA);羟基硅油在25℃下的粘度为500cp;碳纳米管的直径为100nm,长径比为500。
制备方法与实施例1相同。
对比例2
一种用于鞋材的聚醚酯型TPU,由包括以下质量份数的原料组成:
其中多元醇为聚四氢呋喃二醇多元醇(PTMG);羟基硅油在25℃下的粘度为500cp;碳纳米管的直径为100nm,长径比为500。
制备方法与实施例1相同。
对比例3
一种用于鞋材的聚醚酯型TPU,由包括以下质量份数的原料组成:
其中多元醇为聚四氢呋喃二醇/聚己二酸乙二醇酯二醇聚醚酯多元醇(PTMG/PEGA);羟基硅油在25℃下的粘度为500cp。
制备方法与实施例1相同。
上述实施例与对比例所得的弹性体颗粒通过注塑转化成测试样品,测定其力学性能、耐水解性能、磨耗。拉伸强度、撕裂强度、断裂伸长率、邵氏硬度以及磨耗分别按照GB/T529—2009、GB/T 529—2009、GB/T529—1991、GB/T 531—1992以及DIN53516GB9867进行测试,测试结果见表1。耐水解性能测试标准按照GB/T 12000-2003,测试结果见表2。
表1实施例1-5和对比例1-3产品力学性能测试结果
表2实施例1-5和对比例1-3产品耐水解性能测试结果
项目 7d保持率/% 14d保持率/% 21d保持率/% 28d保持率/%
实施例1 77 69 64 57
实施例2 78 67 66 58
实施例3 77 69 63 53
实施例4 75 68 61 54
实施例5 78 68 63 56
对比例1 70 35 20
对比例2 75 70 64 57
对比例3 77 70 62 55
由表1和表2的结果可知,本发明通过选用聚醚酯多元醇制备TPU,并配合羟基硅油、碳纳米管以及其他原料作用,在保持了较高的拉伸强度和断裂伸长率的同时赋予材料良好的耐水解性能和耐磨性满足鞋材产品要求。
申请人声明,以上所述仅为本发明的具体实施方式,但本发明的保护范围并不局限于此,所属技术领域的技术人员应该明了,任何属于本技术领域的技术人员在本发明揭露的技术范围内,可轻易想到的变化或替换,均落在本发明的保护范围和公开范围之内。

Claims (10)

1.一种用于鞋材的聚醚酯型TPU,其特征在于:由下列质量份数的物质组成:
二异氰酸酯为二苯基甲烷二异氰酸酯、氢化苯基甲烷二异氰酸酯或六亚甲基二异氰酸酯中一种或几种。
2.根据权利要求1所述的用于鞋材的聚醚酯型TPU,其特征在于:聚醚酯多元醇的分子量为1000-2000,酯基与醚基的摩尔比为0.8-1.2。
3.根据权利要求2所述的用于鞋材的聚醚酯型TPU,其特征在于:聚醚酯多元醇为聚四氢呋喃二醇/聚己二酸乙二醇酯二醇聚醚酯多元醇、聚氧化丙烯二醇/聚己二酸乙二醇酯二醇聚醚酯多元醇或聚乙二醇/聚己二酸乙二醇酯二醇聚醚酯多元醇中一种或几种。
4.根据权利要求1所述的用于鞋材的聚醚酯型TPU,其特征在于:羟基硅油在25℃下粘度为500-5000cps。
5.根据权利要求1所述的用于鞋材的聚醚酯型TPU,其特征在于:碳纳米管直径为50-200nm,长径比为100-500。
6.根据权利要求1所述的用于鞋材的聚醚酯型TPU,其特征在于:扩链剂为1,4-丁二醇、1,6-己二醇、二羟甲基丙酸或二氯二氨基二苯甲烷中的一种或几种。
7.根据权利要求1所述的用于鞋材的聚醚酯型TPU,其特征在于:催化剂为二月桂酸二丁基锡或辛酸亚锡中的一种或两种。
8.一种权利要求1所述的用于鞋材的聚醚酯型TPU的制备方法,其特征在于:包括以下步骤:
1)将质量比例的二异氰酸酯加入到A储料罐中,将质量比例的聚醚酯多元醇和羟基硅油加入到B储料罐中,将质量比例的扩链剂和催化剂加入到C储料罐中,在搅拌条件下,真空脱水,抽注到双螺杆挤出机中;
2)在双螺杆挤出机加料口加入质量比例的碳纳米管,110℃-190℃下,在双螺杆挤出机中反应,造粒得到TPU颗粒。
9.根据权利要求8所述的用于鞋材的聚醚酯型TPU的制备方法,其特征在于:步骤1中,真空脱水温度为90-120℃;搅拌速率为400-800r/min。
10.根据权利要求8所述的用于鞋材的聚醚酯型TPU的制备方法,其特征在于:步骤2中,双螺杆挤出机的喂料段温度为110-120℃,混合段温度为130-150℃,挤出段温度为170-180℃,机头温度为150-160℃。
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