CN111057295A - 一种发泡母粒及其制作方法 - Google Patents

一种发泡母粒及其制作方法 Download PDF

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CN111057295A
CN111057295A CN201911169561.3A CN201911169561A CN111057295A CN 111057295 A CN111057295 A CN 111057295A CN 201911169561 A CN201911169561 A CN 201911169561A CN 111057295 A CN111057295 A CN 111057295A
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宋季岭
瞿进
熊安军
王来宝
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Huaihua Dongqing Technology Co Ltd
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Abstract

本发明公开了一种发泡母粒及其制作方法,包括如下步骤:步骤一、将聚异丁烯切成小片聚异丁烯;步骤二、将聚异丁烯4.5~10.5%,无机发泡剂15~35%,有机发泡剂12~24%,抗氧剂0.1~2.5%,偶联剂1~3%,硬脂酸2~5%、POE20~40%在90℃以下搅拌混匀得到混合料;步骤三、将混合料加入双螺杆挤出机混练后挤出、冷却和切粒即制得发泡母粒。本发明的母粒中有机和无机发泡剂的总比重可提高到50%以上,使用原料种类极少,生产流程短,操作简单,无小分子析出物,可用来增强改性低VOC低挥发的聚烯烃等树脂。

Description

一种发泡母粒及其制作方法
技术领域
本发明涉及化工领域,特别涉及一种发泡母粒及其制作方法。
背景技术
由于发泡在直接使用中会发生粉尘飞扬,污染环境、损害健康。同时,发泡直接参杂在树脂基体中,会因分散不均,界面结合不良等因素,不能充分发挥其对树脂的增强作用。这些均影响了发泡的使用。
所以发泡的使用通常需要事先对其进行密炼造粒处理。为了进一步提高发泡成份在其母粒中所占比重,减少其它添加剂的使用,提升发泡母粒的性价比,本专利提出一种以聚异丁烯为载体的发泡母粒。
发明内容
本发明的目的是克服现有技术的不足之外,本发明的母粒中有机和无机发泡剂的总比重可提高到50%以上,使用原料种类极少,生产流程短,操作简单,无小分子析出物,可用来增强改性低VOC低挥发的聚烯烃等树脂。
为实现上述目的,本发明采用的技术方案如下:
一种发泡母粒,包括聚异丁烯4.5~10.5%,无机发泡剂15~35%,有机发泡剂12~24%,抗氧剂0.1~2.5%,偶联剂1~3%,硬脂酸2~5%、POE20~40%。
进一步的改进,所述聚异丁烯分子量为20000-65000。
进一步的改进,所述无机发泡剂为碳酸氢钠。
进一步的改进,所述有机发泡剂为2、2,2′-偶氮二异丁腈。
进一步的改进,所述抗氧剂为烷基吩噻嗪,偶联剂为硅烷偶联剂。
一种发泡母粒的制作方法,包括如下步骤:
步骤一、将聚异丁烯切成小片聚异丁烯;
步骤二、将聚异丁烯4.5~10.5%,无机发泡剂15~35%,有机发泡剂12~24%,抗氧剂0.1~2.5%,偶联剂1~3%,硬脂酸2~5%、POE20~40%在90℃以下搅拌混匀得到混合料;
步骤三、将混合料加入双螺杆挤出机混练后挤出、冷却和切粒即制得发泡母粒。
进一步的改进,所述步骤三中,挤出温度控制在90~100℃;挤出后的料条经过室温的空气冷却,定型后切粒。
进一步的改进,所述步骤一中,不定形态的聚异丁烯放入压片机,挤出成片后切成厚度为1mm、面积为≤1cm2的小片聚异丁烯。
具体实施方式
本发明的制作工艺如下:
1.不定形态的聚异丁烯放入压片机,挤出成片后切成厚度为1mm、面积为1cm2左右的小片;或加热到80℃左右到熔融状态后加入到密炼机或高混机中;
2.将聚异丁烯小片与发泡剂等助剂混合,后加入到高速搅拌机中,加热到70℃,并保持搅拌15min;
3.将搅拌混合好的原料投入到双螺杆挤出机,挤出温度控制在90~100℃左右;挤出后的料条经过室温的空气冷却,定型后切粒。
实施例1
一种发泡母粒的制作方法,包括如下步骤:
步骤一、将不定形态聚异丁烯经过压片机后切成小块聚异丁烯;
步骤二、将聚异丁烯10.5%,无机发泡剂35%,有机发泡剂24%,抗氧剂2.5%,偶联剂3%,硬脂酸5%、POE20%90℃以下搅拌混匀得到混合料;
步骤三、将混合料加入双螺杆挤出机混练后挤出、冷却和切粒即制得发泡母粒。
实施例2
一种发泡母粒的制作方法,包括如下步骤:
步骤一、将不定形态聚异丁烯经过压片机后切成小块聚异丁烯;
步骤二、将聚异丁烯10.5%,无机发泡剂15%,有机发泡剂24%,抗氧剂2.5%,偶联剂3%,硬脂酸5%、POE40%重量份90℃以下搅拌混匀得到混合料;
步骤三、将混合料加入双螺杆挤出机混练后挤出、冷却和切粒即制得发泡母粒。
实施例3
一种发泡母粒的制作方法,包括如下步骤:
步骤一、将不定形态聚异丁烯经过压片机后切成小块聚异丁烯;
步骤二、将聚异丁烯8%,无机发泡剂28%,有机发泡剂22%,抗氧剂0.1%,偶联剂1%,硬脂酸2%、POE38.9%90℃以下搅拌混匀得到混合料;
步骤三、将混合料加入双螺杆挤出机混练后挤出、冷却和切粒即制得发泡母粒。
实施例4
一种发泡母粒的制作方法,包括如下步骤:
步骤一、将不定形态聚异丁烯经过压片机后切成小块聚异丁烯;
步骤二、将聚异丁烯8%,无机发泡剂31%,有机发泡剂21%,抗氧剂0.5%,偶联剂2%,硬脂酸3%、POE34.5%90℃以下搅拌混匀得到混合料;
步骤三、将混合料加入双螺杆挤出机混练后挤出、冷却和切粒即制得发泡母粒。
上述四种产品的性能如下:
Figure BDA0002286655290000041
因此实施例4为最佳实施例,在保证产品性能的情况下大大提高了发泡剂的负载量。
上述实施例仅为最佳例举,而并非是对本发明的实施方式的限定。

Claims (8)

1.一种发泡母粒,其特征在于,包括聚异丁烯4.5~10.5%,无机发泡剂15~35%,有机发泡剂12~24%,抗氧剂0.1~2.5%,偶联剂1~3%,硬脂酸2~5%、POE20~40%。
2.如权利要求1所述的发泡母粒,其特征在于,所述聚异丁烯分子量为20000-65000。
3.如权利要求1所述的发泡母粒,其特征在于,所述无机发泡剂为碳酸氢钠。
4.如权利要求1所述的发泡母粒,其特征在于,所述有机发泡剂为2、2,2′-偶氮二异丁腈。
5.如权利要求1所述的发泡母粒,其特征在于,所述抗氧剂为烷基吩噻嗪,偶联剂为硅烷偶联剂。
6.一种发泡母粒的制作方法,其特征在于,包括如下步骤:
步骤一、将聚异丁烯切成小片聚异丁烯;
步骤二、将聚异丁烯4.5~10.5%,无机发泡剂15~35%,有机发泡剂12~24%,抗氧剂0.1~2.5%,偶联剂1~3%,硬脂酸2~5%、POE20~40%在90℃以下搅拌混匀得到混合料;
步骤三、将混合料加入双螺杆挤出机混练后挤出、冷却和切粒即制得发泡母粒。
7.如权利要求6所述的发泡母粒的制作方法,其特征在于,所述步骤三中,挤出温度控制在90~100℃;挤出后的料条经过室温的空气冷却,定型后切粒。
8.如权利要求6所述的发泡母粒的制作方法,其特征在于,所述步骤一中,不定形态的聚异丁烯放入压片机,挤出成片后切成厚度为1mm、面积为≤1cm2的小片聚异丁烯。
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