CN102702715A - 一种高流动性玻纤增强无卤阻燃pc树脂及其制备方法 - Google Patents
一种高流动性玻纤增强无卤阻燃pc树脂及其制备方法 Download PDFInfo
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Abstract
本发明涉及PC树脂改性技术领域,特别是涉及一种高流动性玻纤增强无卤阻燃PC树脂及其制备方法,该种高流动性玻纤增强无卤阻燃PC树脂,它由以下重量百分比的原料组成:PC树脂30-70%、玻璃纤维10-35%、AS树脂5-30%、阻燃剂8-15%、增韧剂5-10%、抗氧剂0.2-1.5%,以上原料经共混挤出造粒制得,本发明制得的种高流动性玻纤增强无卤阻燃PC在满足材料UL94V0阻燃的基础上,耐热性、加工流动性、抗冲击性能优异;本发明的制备方法工艺简单、成本低。
Description
技术领域
本发明涉及PC树脂改性技术领域,特别是涉及一种高流动性玻纤增强无卤阻燃PC树脂及其制备方法。
背景技术
聚碳酸酯PC具有冲击强度高,透明,无毒,介电性能优良抗蠕变性和尺寸稳定性等优点,在电气,汽车工业,医疗器械,建筑和照明用具等领域已广泛应用。虽然聚碳酸酯PC的阻燃等级为UL94-V-2。但是仍可燃烧,且燃烧时有热熔体滴下,容易引起附近材料着火,难以满足阻燃防火要求。因此,在实际应用中要对PC进行阻燃处理。
如专利号为ZL200810038154.4的中国发明公开了一种低发烟量无卤阻燃PC/ABS合金及其制备方法,按重量百分比称取聚碳酸酯(PC)40-75%,丙烯晴-丁二烯-苯乙烯共聚物(ABS)10-40%,复合阻燃剂10-15%,复合降烟剂0.2-2%,相容剂2-16%,低发烟促进剂1-6%,稳定剂0.1-0.5%,润滑剂0.1-0.6%,以上专利和其它现有技术要使PC树脂达到V0级别阻燃,都添加了很大量的阻燃剂和其它助剂,导致改性PC树脂的耐热性急剧下降,加工流动性较差。
发明内容
本发明的目的在于针对现有技术的不足,提供了一种高流动性玻纤增强无卤阻燃PC树脂及其制备方法,该种高流动性玻纤增强无卤阻燃PC树脂耐热性好、加工流动性强,该种高流动性玻纤增强无卤阻燃PC树脂的制备方法工艺简单、成本低。
本发明的目的是这样实现的:一种高流动性玻纤增强无卤阻燃PC树脂,它由以下重量百分比的原料组成:
PC树脂 30-70%
玻璃纤维 10-35%
AS树脂 5-30%
阻燃剂 8-15%
增韧剂 5-10%
抗氧剂 0.2-1.5%。
优选的,它由以下重量百分比的原料组成:
PC树脂 30-64%
玻璃纤维 15-35%
AS树脂 5-30%
阻燃剂 10-15%
增韧剂 5-10%
抗氧剂 1-1.5%。
更为优选的,它由以下重量百分比的原料组成:
PC树脂 45%
玻璃纤维 15%
AS树脂 19%
阻燃剂 15%
增韧剂 5%
抗氧剂 1%。
其中,所述PC树脂为一种通用型号芳香族聚碳酸酯,密度为1.1-1.6g/cm3。
其中,所述玻璃纤维的直径为10μm-13μm。
其中,所述AS树脂中苯乙烯含量为30%-50%。
其中,所述阻燃剂为双酚A双(磷酸二苯酯)(BDP)。
其中,所述增韧剂为甲基丙烯酸甲酯、丁二烯、及苯乙烯的三元共聚物(MBS)。
其中,所述抗氧剂为四[β-(3,5-二叔丁基-4-羟基苯基)丙酸]季戊四醇酯,三[2.4-二叔丁基苯基]亚磷酸酯,2-叔丁基-6-(3-叔丁基-5-甲基-2-羟苯基)-4-甲基苯基丙烯酸酯中的一种或任意几种。
本发明通过调节玻璃纤维的含量来有效改善材料的耐热性能,通过调节AS树脂的含量来有效改善材料的加工流动性。
上述高流动性玻纤增强无卤阻燃PC树脂的制备方法,它包括以下制备步骤:
步骤A、将PC 树脂和AS树脂在80℃烘烤1小时,备用;
步骤B、将烘烤后的PC树脂、将烘烤后的AS树脂、阻燃剂、增韧剂、抗氧剂按比例加入高速混合机中高速共混5-10min,得到共混物;
步骤C、将玻璃纤维和步骤B得到的共混物经双螺杆挤出机挤出造粒;
步骤D、将步骤C得到的粒子在100℃ 烘烤1-2小时,即得成品。
其中,所述步骤C双螺杆挤出机的具体工艺参数为:一区温度 210-200℃,二区温度210-200℃,三区温度210-200℃,四区温度210-200℃,五区温度210-200℃,六区温度 190-200℃,七区温度190-200℃,八区温度190-200℃,九区温度190-200℃,模头温度190-195℃ ,停留时间2-3min,压力12-18MPa,螺杆转速 280-350R/min。
本发明的有益效果为:本发明制备的高流动性玻纤增强无卤阻燃PC树脂,在满足材料UL94 V0阻燃的基础上,耐热性、加工流动性、抗冲击性能优异;本发明的制备方法工艺简单、成本低。
具体实施方式
下面通过实施例对本发明作进一步说明,但本发明的实施范围并不限于此。
实施例1。
将PC 树脂和AS树脂在80℃烘烤1小时,然后将30㎏烘烤后的PC树脂、将30㎏烘烤后的AS树脂、15㎏BDP、5㎏MBS、0.2㎏四[β-(3,5-二叔丁基-4-羟基苯基)丙酸]季戊四醇酯加入高速混合机中高速共混10min,得到共混物,再将19.8㎏玻璃纤维和上述共混物经双螺杆挤出机挤出造粒,得到的粒子在100℃ 烘烤2小时,即得成品。双螺杆挤出机的具体工艺参数为:一区温度 210℃,二区温度200℃,三区温度205℃,四区温度210℃,五区温度200℃,六区温度 195℃,七区温度200℃,八区温度190℃,九区温度200℃,模头温度195℃ ,停留时间2min,压力12MPa,螺杆转速 280R/min。
实施例2。
将PC 树脂和AS树脂在80℃烘烤1小时,然后将70㎏烘烤后的PC树脂、将5㎏烘烤后的AS树脂、8.5㎏BDP、5㎏MBS、0.5㎏四[β-(3,5-二叔丁基-4-羟基苯基)丙酸]季戊四醇酯、0.5㎏三[2.4-二叔丁基苯基]亚磷酸酯、0.5㎏2-叔丁基-6-(3-叔丁基-5-甲基-2-羟苯基)-4-甲基苯基丙烯酸酯加入高速混合机中高速共混8min,得到共混物,再将10㎏玻璃纤维和上述共混物经双螺杆挤出机挤出造粒,得到的粒子在100℃ 烘烤1小时,即得成品。双螺杆挤出机的具体工艺参数为:一区温度200℃,二区温度210℃,三区温度200℃,四区温度210℃,五区温度200℃,六区温度 190℃,七区温度200℃,八区温度190℃,九区温度200℃,模头温度195℃ ,停留时间3min,压力18MPa,螺杆转速350R/min。
实施例3。
将PC 树脂和AS树脂在80℃烘烤1小时,然后将50㎏烘烤后的PC树脂、将20㎏烘烤后的AS树脂、10㎏BDP、5.8㎏MBS、0.2㎏三[2.4-二叔丁基苯基]亚磷酸酯加入高速混合机中高速共混8min,得到共混物,再将14㎏玻璃纤维和上述共混物经双螺杆挤出机挤出造粒,得到的粒子在100℃ 烘烤2小时,即得成品。双螺杆挤出机的具体工艺参数为:一区温度 205℃,二区温度200℃,三区温度205℃,四区温度210℃,五区温度205℃,六区温度 195℃,七区温度200℃,八区温度195℃,九区温度195℃,模头温度190℃ ,停留时间2min,压力15MPa,螺杆转速 320R/min。
实施例4。
将PC 树脂和AS树脂在80℃烘烤1小时,然后将45㎏烘烤后的PC树脂、将19㎏烘烤后的AS树脂、15㎏BDP、5㎏MBS、1㎏2-叔丁基-6-(3-叔丁基-5-甲基-2-羟苯基)-4-甲基苯基丙烯酸酯加入高速混合机中高速共混8min,得到共混物,再将15㎏玻璃纤维和上述共混物经双螺杆挤出机挤出造粒,得到的粒子在100℃ 烘烤2小时,即得成品。双螺杆挤出机的具体工艺参数为:一区温度 210℃,二区温度200℃,三区温度210℃,四区温度208℃,五区温度210℃,六区温度 198℃,七区温度195℃,八区温度200℃,九区温度190℃,模头温度193℃ ,停留时间3min,压力18MPa,螺杆转速 330R/min。
实施例5。
将PC 树脂和AS树脂在80℃烘烤1小时,然后将40㎏烘烤后的PC树脂、将10㎏烘烤后的AS树脂、10㎏BDP、10㎏MBS、0.5㎏四[β-(3,5-二叔丁基-4-羟基苯基)丙酸]季戊四醇酯、0.5㎏三[2.4-二叔丁基苯基]亚磷酸酯加入高速混合机中高速共混10min,得到共混物,再将29㎏玻璃纤维和上述共混物经双螺杆挤出机挤出造粒,得到的粒子在100℃ 烘烤1小时,即得成品。双螺杆挤出机的具体工艺参数为::一区温度 205℃,二区温度200℃,三区温度205℃,四区温度210℃,五区温度205℃,六区温度 195℃,七区温度200℃,八区温度195℃,九区温度195℃,模头温度190℃ ,停留时间2min,压力15MPa,螺杆转速 320R/min。
实施例6。
将PC 树脂和AS树脂在80℃烘烤1小时,然后将40㎏烘烤后的PC树脂、将15㎏烘烤后的AS树脂、13.5㎏BDP、5㎏MBS、1㎏四[β-(3,5-二叔丁基-4-羟基苯基)丙酸]季戊四醇酯、0.5㎏2-叔丁基-6-(3-叔丁基-5-甲基-2-羟苯基)-4-甲基苯基丙烯酸酯加入高速混合机中高速共混5min,得到共混物,再将25㎏玻璃纤维和上述共混物经双螺杆挤出机挤出造粒,得到的粒子在100℃ 烘烤2小时,即得成品。双螺杆挤出机的具体工艺参数为:一区温度200℃,二区温度210℃,三区温度200℃,四区温度210℃,五区温度200℃,六区温度 190℃,七区温度200℃,八区温度190℃,九区温度200℃,模头温度195℃ ,停留时间3min,压力17MPa,螺杆转速340R/min。
说明:实施例1-6所用的PC树脂为一种通用型号芳香族聚碳酸酯,密度为1.1-1.6g/cm3;玻璃纤维的直径为10μm-13μm;AS树脂中苯乙烯含量为30%-50%;阻燃剂为双酚A双(磷酸二苯酯)(BDP);增韧剂为甲基丙烯酸甲酯、丁二烯、及苯乙烯的三元共聚物(MBS)。
本发明产品的性能评价方式及实行标准:
按照上述方法完成造粒的粒子放入80℃的鼓风烘箱中干燥1-2小时,然后再将干燥好的粒子在注射成型机上进行注射成型制样。
拉伸性能测试按ISO-527-2进行,试样尺寸150*10*4mm ,拉伸速度为50mm/min;弯曲强度按ISO 178进行,试样尺寸80*10*4mm ,弯曲速度为2mm/min,跨距为64mm;
简支梁冲击强度按ISO 179进行,试样尺寸80*6*4mm,缺口深度为试样厚度的三分之一;
热变形温度按ISO 75进行,试样尺寸120*10*3mm,载荷为1.8MPa;
熔融指数按照ISO1133,试样为粒子状,加工流动性通过熔融指数进行评价。
实施例1-6产品性能参数见表1。
通过表1可以看出本发明制备的高流动性玻纤增强无卤阻燃PC树脂耐热性、加工流动性、抗冲击性能优异。
最后应当说明的是,以上实施例仅用以说明本发明的技术方案,而非对本发明保护范围的限制,尽管参照较佳实施例对本发明作了详细地说明,本领域的普通技术人员应当理解,可以对本发明的技术方案进行修改或者等同替换,而不脱离本发明技术方案的实质和范围。
Claims (10)
1.一种高流动性玻纤增强无卤阻燃PC树脂,其特征在于: 它由以下重量百分比的原料组成:
PC树脂 30-70%
玻璃纤维 10-35%
AS树脂 5-30%
阻燃剂 8-15%
增韧剂 5-10%
抗氧剂 0.2-1.5%。
2.根据权利要求1所述的一种高流动性玻纤增强无卤阻燃PC树脂,其特征在于:它由以下重量百分比的原料组成:
PC树脂 30-64%
玻璃纤维 15-35%
AS树脂 5-30%
阻燃剂 10-15%
增韧剂 5-10%
抗氧剂 1-1.5%。
3.根据权利要求2所述的一种高流动性玻纤增强无卤阻燃PC树脂,其特征在于:它由以下重量百分比的原料组成:
PC树脂 45%
玻璃纤维 15%
AS树脂 19%
阻燃剂 15%
增韧剂 5%
抗氧剂 1%。
4.根据权利要求1-3任一项所述的一种高流动性玻纤增强无卤阻燃PC树脂,其特征在于:所述玻璃纤维的直径为10μm-13μm。
5.根据权利要求1-3任一项所述的一种高流动性玻纤增强无卤阻燃PC树脂,其特征在于:所述AS树脂中苯乙烯含量为30%-50%。
6.根据权利要求1-3任一项所述的一种高流动性玻纤增强无卤阻燃PC树脂,其特征在于:所述阻燃剂为双酚A双(磷酸二苯酯)。
7.根据权利要求1-3任一项所述的一种高流动性玻纤增强无卤阻燃PC树脂,其特征在于:所述增韧剂为甲基丙烯酸甲酯、丁二烯及苯乙烯的三元共聚物。
8.根据权利要求1-3任一项所述的一种高流动性玻纤增强无卤阻燃PC树脂,其特征在于:所述抗氧剂为四[β-(3,5-二叔丁基-4-羟基苯基)丙酸]季戊四醇酯,三[2.4-二叔丁基苯基]亚磷酸酯,2-叔丁基-6-(3-叔丁基-5-甲基-2-羟苯基)-4-甲基苯基丙烯酸酯中的一种或任意几种。
9.权利要求1-8任一项所述的高流动性玻纤增强无卤阻燃PC树脂的制备方法,其特征在于:它包括以下制备步骤:
步骤A、将PC 树脂和AS树脂在80℃烘烤1小时,备用;
步骤B、将烘烤后的PC树脂、将烘烤后的AS树脂、阻燃剂、增韧剂、抗氧剂按比例加入高速混合机中高速共混5-10min,得到共混物;
步骤C、将玻璃纤维和步骤B得到的共混物经双螺杆挤出机挤出造粒;
步骤D、将步骤C得到的粒子在100℃ 烘烤1-2小时,即得成品。
10.根据权利要求9所述的一种高流动性玻纤增强无卤阻燃PC的制备方法,其特征在于:所述步骤C双螺杆挤出机的具体工艺参数为:一区温度 210-200℃,二区温度210-200℃,三区温度210-200℃,四区温度210-200℃,五区温度210-200℃,六区温度 190-200℃,七区温度190-200℃,八区温度190-200℃,九区温度190-200℃,模头温度190-195℃ ,停留时间2-3min,压力12-18MPa,螺杆转速 280-350R/min。
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