CN105153390A - 环保型聚氨酯发泡轮胎组合料及其制备方法 - Google Patents
环保型聚氨酯发泡轮胎组合料及其制备方法 Download PDFInfo
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Abstract
本发明属于聚氨酯技术领域,具体涉及一种环保型聚氨酯发泡轮胎组合料及其制备方法。由A组分与B组分按质量比为100:85-105混合制成:A组分由聚醚多元醇、聚合物多元醇、扩链剂、交联剂、泡孔稳定剂、发泡剂和催化剂制成;B组分是一种聚酯多元醇改性的异氰酸酯组分,由聚酯多元醇、异氰酸酯和储存稳定剂制成。本发明与现有技术的原料相比,发泡剂为水,环保的同时,省去物理发泡剂费用,成本大幅度降低。本发明制备的环保型聚氨酯发泡轮胎在满足硬度的同时,也具有良好的结皮性和光亮的表面。能够用于正常发泡轮胎的生产,是轮胎生产的理想替代材料。本发明还提供其制备方法,工艺合理。
Description
技术领域
本发明属于聚氨酯技术领域,具体涉及一种环保型聚氨酯发泡轮胎组合料及其制备方法。
背景技术
聚氨酯发泡轮胎以其良好的耐磨性、优良的耐酸碱性及耐针扎,越来越被大家接受。目前被广泛应用于货物推车、童车、慢速电动车等领域。
专利CN102250313A报道了一种用于聚氨酯发泡轮胎的自结皮微孔弹性体组合物,此发明制备的聚氨酯发泡轮胎具有优异的力学性能、良好的回弹性以及优异的耐水解性和耐霉菌性。但是,其用的发泡剂为物理发泡剂—HCFC-141b,141b中含有氯原子,对臭氧层有破坏作用。发达国家已于2010年全面禁止使用141b。戊烷、HFC-365mfc、HFC-245fa等试剂作为141b的替代品,虽然都是零DOP,但是不同试剂在应用过程中存在不同问题。例如:戊烷虽然成本低廉、发泡率与141b相近,但是其易燃易爆的特点,使得运输、生产操作过程中要求极其严格,不利于正常生产使用。因此以上提到的试剂只是过渡品,水发泡才是最终替代品。
专利CN10331985A报道了一种自结皮聚氨酯泡沫塑料及制备方法。此发明用水发泡,具体应用于汽车方向盘、扶手、仪表板等静态自结皮聚氨酯。采用水发泡优点为成本低、与异氰酸酯生成二氧化碳对大气无害、生产现场气味低,无易燃性。但是与正常物理发泡剂(141b)相比,水发泡的制品也存在很明显的缺点:表皮薄,性能差。
发明内容
针对现有技术的不足,本发明的目的是提供一种环保型聚氨酯发泡轮胎组合料,用于制备聚氨酯发泡轮胎,在满足硬度的同时,也具有良好的结皮性和光亮的表面;本发明还提供其制备方法。
本发明所述的环保型聚氨酯发泡轮胎组合料,由A组分与B组分按质量比为100:85-105混合制成:
A组分由以下质量份数的原料制成:
B组分由以下质量分数的原料制成:
聚酯多元醇:15-30%
异氰酸酯:70-85%
储存稳定剂:10ppm。
其中:
B组分是由聚酯多元醇改性的异氰酸酯组分。B组分的-NCO的质量含量在22-27%之间。
A组分中的聚醚多元醇平均官能度为2-4,优选2-3,数均分子量为1000-8000,优选2000-6000,伯羟基质量含量≥75%,不饱和度≤0.008meq/g;优选EP-330NG(市售,山东蓝星东大化工有限责任公司)、FA-703(市售,可利亚聚醚多元醇南京有限公司)或EP-3600(市售,山东蓝星东大化工有限责任公司)中的一种或几种。
A组分中的聚合物多元醇为以乙烯基聚醚三醇为基础聚醚,用苯乙烯或丙烯腈接枝共聚,固含量≥30%的聚合物多元醇。优选POP93/28(市售,山东蓝星东大化工有限责任公司)、POP36/28(市售,山东蓝星东大化工有限责任公司)或POP40(市售,山东蓝星东大化工有限责任公司)中的一种或几种。
A组分中的扩链剂为乙二醇、丙二醇、1,4-丁二醇或一缩二丙二醇中的一种或几种的混合物。
A组分中的交联剂为甘油、二乙醇胺、三乙醇胺或三羟甲基丙烷中的一种或几种的混合物。
A组分中的发泡剂为水。
A组分中的泡沫稳定剂为聚硅氧烷-氧化烯烃嵌段共聚物,优选DC6070(市售,美国空气化工产品有限公司)、AK-7703(市售,南京德美世创化工有限公司)和DC3043(市售,美国空气化工产品有限公司)中的一种或几种。
A组分中的催化剂为叔胺类催化剂或有机锡类催化剂中的一种或几种;叔胺类催化剂优选A-33(市售)、A-1(市售)或C-225(市售,美国,GE公司),有机锡类催化剂优选CS-12(市售)。
B组分中的异氰酸酯为纯MDI、碳化二亚胺改性MDI或MDI-50中的一种或几种的混合物。
B组分中的聚酯多元醇优选PE-2420或CMA-244中的一种或两种混合物;PE-2420为山东一诺威聚氨酯股份有限公司市售产品,CMA-244为华大化学集团有限公司市售产品。
B组分中的储存稳定剂为磷酸。
本发明所述的环保型聚氨酯发泡轮胎组合料的制备方法,包括以下步骤:
A组分:先将聚醚多元醇和聚合物多元醇投入反应釜中搅拌,然后依次加入扩链剂、交联剂、催化剂、泡沫稳定剂和发泡剂,在室温条件下,搅拌1-2小时后密封保存;
B组分:将聚酯多元醇常温下投入反应釜中,搅拌升温至90-100℃,真空条件下脱水脱气2-3小时,然后降温至40℃,加入异氰酸酯,在80-85℃反应2-3小时,-NCO的质量含量达到22-27%之间,降温至40-50℃,密封保存。
使用时,将A、B料置于低压浇注机对应罐中,按A组分与B组分按质量比为100:85-105的比例浇注到动态轮胎模具中,三分钟左右开模,修剪、排气。静置1小时左右,制备得到环保型聚氨酯发泡轮胎,硬度在邵A85-95。
综上所述,本发明具有以下优点:
(1)本发明与现有技术的原料相比,发泡剂为水,环保的同时,省去物理发泡剂费用,成本有大幅度降低。
(2)现有技术使用141b,由于141b极易挥发,使用过程中不可避免被现场工人吸入、甚至接触,一旦在体内分解,将严重影响身体健康,且对臭氧层有破坏作用。而本发明采用水发泡避免了这一问题,水与异氰酸酯生成二氧化碳对大气无害。
(3)本发明制备的环保型聚氨酯发泡轮胎在满足硬度的同时,也具有良好的结皮性和光亮的表面。能够用于正常发泡轮胎的生产,是轮胎生产的理想替代材料。
具体实施方式
下面结合实施例对本发明做进一步说明。
实施例1
A组分:分别称取EP-330NG90Kg和POP36/2810Kg投入反应釜中搅拌,然后依次加入1,4-丁二醇7Kg,乙二醇13Kg,甘油1.0kg,A-331.5Kg,AK-77030.2Kg,DC-1930.2Kg,水0.5Kg。在30℃下搅拌1小时,充分混合均匀,密封保存,备用。
B组分:称取PE-242010Kg置于釜中,搅拌升温至100℃,真空条件下脱水脱气2小时。然后降温至40℃,开搅拌加入4,4’-二苯基甲烷二异氰酸酯30Kg,碳化二亚胺改性MDI3Kg,缓慢升温至85℃,保温反应1.5小时。搅拌20分钟,取样检测,合格后冲N2放料,备用。
使用时,A、B料温维持在35-40℃,按A组分与B组分按质量比为100:94的比例浇注到动态轮胎模具中,模具温度50-55℃,3分钟开模,修边、排气后。自然熟化,1小时左右制备得到聚氨酯发泡轮胎。
实施例2
A组分:分别称取EP360090Kg和POP36/2810Kg投入反应釜中搅拌,然后依次加入丙二醇14Kg,乙二醇6Kg,二乙醇胺0.5kg,A-10.5kg,A-33:0.8Kg,CS-120.05kg,AK-77030.2Kg,DC60700.2Kg,水0.6Kg。在30℃下搅拌2小时,充分混合均匀,密封保存,备用。
B组分:称取CMA-24415Kg置于釜中,搅拌升温至90℃,真空条件下脱水脱气3小时。然后降温至40℃,开搅拌加入4,4’-二苯基甲烷二异氰酸酯30Kg,碳化二亚胺改性MDI10Kg,缓慢升温至85℃,保温反应1.5小时。搅拌20分钟,取样检测,合格后冲N2放料,备用。
使用时,A、B料温维持在35-40℃,按A组分与B组分按质量比为100:92的比例浇注到动态轮胎模具中,模具温度50-55℃,3分钟开模,修边、排气后。自然熟化,1小时左右制备得到聚氨酯发泡轮胎。
实施例3
A组分:分别称取EP-330NG80Kg和POP93/2820Kg投入反应釜中搅拌,然后依次加入1,4-丁二醇7Kg,乙二醇6Kg,三乙醇胺1.5kg,A-331.5Kg,AK-77030.3Kg,DC60700.3Kg,水0.5Kg。在30℃下搅拌1小时,充分混合均匀,密封保存,备用。
B组分:称取PE-242010Kg置于釜中,搅拌升温至95℃,真空条件下脱水脱气2.5小时。然后降温至40℃,开搅拌加入4,4’-二苯基甲烷二异氰酸酯30Kg,碳化二亚胺改性MDI10Kg,缓慢升温至82℃,保温反应1.5小时。搅拌20分钟,取样检测,合格后冲N2放料,备用。
使用时,A、B料温维持在35-40℃,按A组分与B组分按质量比为100:93的比例浇注到动态轮胎模具中,模具温度50-55℃,3分钟开模,修边、排气后。自然熟化,1小时左右制备得到聚氨酯发泡轮胎。
对比例
采用与实施例1相同的制备方法,唯一的不同是发泡剂采用141b体系配方。
将实施例1-3和对比例制备得到的聚氨酯发泡轮胎进行性能测试,测试结果见表1。
表1实施例1-3和对比例制备得到的聚氨酯发泡轮胎的性能测试结果
由表1可以看出,本发明制备的环保型聚氨酯发泡轮胎在满足硬度的同时,也具有良好的结皮性和光亮的表面。能够用于正常发泡轮胎的生产,是轮胎生产的理想替代材料。
Claims (10)
1.一种环保型聚氨酯发泡轮胎组合料,其特征在于:由A组分与B组分按质量比为100:85-105混合制成:
A组分由以下质量份数的原料制成:
B组分由以下质量分数的原料制成:
聚酯多元醇:15-30%
异氰酸酯:70-85%
储存稳定剂:10ppm。
2.根据权利要求1所述的环保型聚氨酯发泡轮胎组合料,其特征在于:A组分中的聚醚多元醇平均官能度为2-4,数均分子量为1000-8000,伯羟基质量含量≥75%,不饱和度≤0.008meq/g。
3.根据权利要求1所述的环保型聚氨酯发泡轮胎组合料,其特征在于:A组分中的聚合物多元醇为以乙烯基聚醚三醇为基础聚醚,用苯乙烯或丙烯腈接枝共聚,固含量≥30%的聚合物多元醇。
4.根据权利要求1所述的环保型聚氨酯发泡轮胎组合料,其特征在于:扩链剂为乙二醇、丙二醇、1,4-丁二醇或一缩二丙二醇中的一种或几种的混合物;A组分中的交联剂为甘油、二乙醇胺、三乙醇胺或三羟甲基丙烷中的一种或几种的混合物。
5.根据权利要求1所述的环保型聚氨酯发泡轮胎组合料,其特征在于:A组分中的发泡剂为水。
6.根据权利要求1所述的环保型聚氨酯发泡轮胎组合料,其特征在于:A组分中的泡沫稳定剂为聚硅氧烷-氧化烯烃嵌段共聚物;A组分中的催化剂为叔胺类催化剂或有机锡类催化剂中的一种或几种。
7.根据权利要求1所述的环保型聚氨酯发泡轮胎组合料,其特征在于:B组分中的异氰酸酯为纯MDI、碳化二亚胺改性MDI或MDI-50中的一种或几种的混合物。
8.根据权利要求1所述的环保型聚氨酯发泡轮胎组合料,其特征在于:B组分中的聚酯多元醇优选PE-2420或CMA-244中的一种或两种混合物。
9.根据权利要求1所述的环保型聚氨酯发泡轮胎组合料,其特征在于:B组分中的储存稳定剂为磷酸。
10.一种权利要求1-9任一所述的环保型聚氨酯发泡轮胎组合料的制备方法,其特征在于:包括以下步骤:
A组分:先将聚醚多元醇和聚合物多元醇投入反应釜中搅拌,然后依次加入扩链剂、交联剂、催化剂、泡沫稳定剂和发泡剂,在室温条件下,搅拌1-2小时后密封保存;
B组分:将聚酯多元醇常温下投入反应釜中,搅拌升温至90-100℃,真空条件下脱水脱气2-3小时,然后降温至40℃,加入异氰酸酯,在80-85℃反应2-3小时,-NCO的质量含量达到22-27%之间,降温至40-50℃,密封保存。
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