CN106751043A - 一种高强度、高热稳定性的聚4‑甲基‑1‑戊烯微孔膜及其制备方法 - Google Patents
一种高强度、高热稳定性的聚4‑甲基‑1‑戊烯微孔膜及其制备方法 Download PDFInfo
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Abstract
本发明公开了一种高强度、高热稳定性的聚(4‑甲基‑1‑戊烯)微孔膜及其制备方法。该隔膜由聚(4‑甲基‑1‑戊烯)、抗氧剂和稀释剂组成。其中,聚(4‑甲基‑1‑戊烯)树脂:25~50份;抗氧剂:0.05~1份;稀释剂:50~75份;通过混炼熔融、挤出成型、双向拉伸、萃取干燥、热处理定型等工序制得聚(4‑甲基‑1‑戊烯)微孔膜,本发明的优点在于,相比于聚烯烃隔膜,具有高耐热性、高机械强度及高吸液保液率等优点。用本发明所制备的聚(4‑甲基‑1‑戊烯)微孔膜在105℃/1h时MD方向上热收缩率不大于3.0,TD方向上的热收缩率不大于2.0,MD拉伸强度大于200MPa,TD拉伸强度大于170MPa,透气率范围150±50 sec/100mL。
Description
技术领域
本发明涉及锂离子隔膜材料,具体为一种高强度、高热稳定性的聚(4-甲基-1-戊烯)微孔膜及其制备方法,本发明属于锂离子二次电池制造技术领域。
背景技术
目前,以热致相分离法制备的锂离子电池的隔膜以PE(聚乙烯)为主,其具有良好的化学稳定性和优异的物理性能,但是,商品化的PE隔膜熔点在150℃以下,高温下,热收缩性能差,在锂离子电池使用的过程中,由于一些原因,造成隔膜被刺穿而穿孔,或者因内部或外部的作用下电池温度升高,隔膜发生热收缩或者融化,锂电池正负极直接接触,从而造成锂电池短路甚至爆炸,致使锂电池的安全使用受到局限。
从锂离子电池使用的安全性考虑,隔膜企业纷纷开始研发高强度、高热稳定性的锂电池隔膜,从而保证锂电池能在较高温度下的安全使用。
聚(4-甲基-1-戊烯)(以下简称TPX),TPX是其商品名,TPX具有耐高温、维卡软化点195℃左右、熔点高达240℃、较高的机械强度、高温下耐蠕变性等优良特性,耐环境和耐化学性能好,受到了锂电池行业的注意。
发明内容
本发明旨在克服上述缺点,提供一种高强度、高热稳定性的TPX微孔膜及其制备方法。
本发明的目的是通过以下技术措施实现的:
一种高强度、高热稳定性的TPX微孔膜,由聚(4-甲基-1-戊烯)树脂以及稀释剂和抗氧剂组成,其重量份数为:
聚(4-甲基-1-戊烯)树脂:25~50份;
抗氧剂:0.05~1份;
稀释剂:50~75份。
所述TPX分子量为1×104~1×107;
所述TPX结晶度为30-60%;
所述抗氧剂为受阻酚、抗氧剂168、抗氧剂1010、抗氧剂CA、胺类抗氧剂或有机硫化物的一种或两种以上的混合物;
所述稀释剂为十氢萘、矿物油、石蜡油中的至少一种;
一种高强度、高热稳定性TPX微孔膜的制备方法,包括如下步骤:
(1)将TPX粒料、抗氧剂及稀释剂按一定的重量比加入到挤出机,挤出机工作温度为200~350℃;挤出机螺杆转速为50~300rpm/min;输出压力为10~60MPa,;塑化混炼得到混合物I;
(2)步骤(1)所述混合物I经过计量泵和过滤器过滤后输送到模头并挤出,模头温度240~400℃;然后通过冷却辊将熔体冷却制得前驱体膜,冷却辊工作温度为20~90℃;
(3)将前驱体膜进行双向拉伸,双向拉伸倍率为3~15×5~20;
(4)在室温下利用清洗剂对前驱体膜萃取除去稀释剂并干燥,所述清洗剂为醇或卤代烷烃;
(5)将步骤(4)中干燥后的膜经过热处理定型,定型温度为80~140℃,定型时间1~5分钟。
本发明的有益效果在于:
本发明具有连续生产、工艺流程操作简单等优点,本发明所述微孔膜在105℃/1h时MD方向上热收缩率不大于3.0,TD方向上的热收缩率不大于2.0,MD拉伸强度大于200MPa,TD拉伸强度大于170MPa,透气率范围150±50sec/100mL。本发明所生产的微孔膜具有高耐热性、高机械强度及高吸液保液率等优点。
具体实施方式
以下结合具体的实施例来对本发明的内容进一步说明,但是本发明的保护范围并不仅仅局限于实施例所描述的内容。
实施例1
称量50份TPX(分子量为1×105,结晶度为30%),0.05份抗氧剂(抗氧剂1010),50份的石蜡油,将TPX和抗氧剂按比例输送到挤出机,再将石蜡油由辅机输送到挤出机,由挤出机塑化混溶形成TPX混合熔体,通过冷却辊铸片成片材,经双向拉伸、萃取干燥、热处理定型后得到TPX微孔膜,其中挤出机工作温度240℃,模头温度280℃,螺杆转速50rpm/min,输出压力为15Mpa,冷却辊温度60℃,双向拉伸倍率为8×10倍,定型温度120℃,定型时间1min,产品性能见表1。
实施例2
称量25份TPX(分子量为5×106,结晶度为60%),1份抗氧剂(抗氧剂168),75份的石蜡油,将TPX和抗氧剂按比例输送到挤出机,再将石蜡油由辅机输送到挤出机,由挤出机塑化混溶形成TPX混合熔体,通过冷却辊铸片成片材,经双向拉伸、萃取干燥、热处理定型后得到TPX微孔膜,其中挤出机工作温度280℃,模头温度300℃,螺杆转速150rpm/min,输出压力为45Mpa,冷却辊温度60℃,双向拉伸倍率为8×10倍,定型温度120℃,定型时间1min,产品性能见表1。
实施例3
称量30份TPX(分子量为2×105,结晶度为35%),0.1份抗氧剂(抗氧剂1010),69.5份的石蜡油,将TPX和抗氧剂按比例输送到挤出机,再将石蜡油由辅机输送到挤出机,由挤出机塑化混溶形成TPX混合熔体,通过冷却辊铸片成片材,经双向拉伸、萃取干燥、热处理定型后得到TPX微孔膜,其中挤出机工作温度240℃,模头温度280℃,螺杆转速50rpm/min,输出压力为25Mpa,冷却辊温度60℃,双向拉伸倍率为8×10倍,定型温度120℃,定型时间1min,产品性能见表1。
实施例4
称量40份TPX(分子量为2×105,结晶度为35%),0.5份抗氧剂(抗氧剂1010),59.5份的矿物油,将TPX和抗氧剂按比例输送到挤出机,再将石蜡油由辅机输送到挤出机,由挤出机塑化混溶形成TPX混合熔体,通过冷却辊铸片成片材,经双向拉伸、萃取干燥、热处理定型后得到TPX微孔膜,其中挤出机工作温度240℃,模头温度280℃,螺杆转速50rpm/min,输出压力为25Mpa,冷却辊温度60℃,双向拉伸倍率为8×10倍,定型温度120℃,定型时间1min,产品性能见表1。
实施例5
称量30份TPX(分子量为5×106,结晶度为50%),0.5份抗氧剂(抗氧剂168),69.5份的矿物油,将TPX和抗氧剂按比例输送到挤出机,再将石蜡油由辅机输送到挤出机,由挤出机塑化混溶形成TPX混合熔体,通过冷却辊铸片成片材,经双向拉伸、萃取干燥、热处理定型后得到TPX微孔膜,其中挤出机工作温度260℃,模头温度300℃,螺杆转速120rpm/min,输出压力为40Mpa,冷却辊温度60℃,双向拉伸倍率为8×10倍,定型温度120℃,定型时间1min,产品性能见表1。
对比例
称量35份PE,0.1份抗氧剂(抗氧剂1010),64.9份的石蜡油,将PE和抗氧剂按比例输送到挤出机,再将石蜡油由辅机输送到挤出机,由挤出机塑化混溶形成PE混合熔体,通过冷却辊铸片成片材,经双向拉伸、萃取干燥、热处理定型后得到PE微孔膜,其中挤出机工作温度240℃,模头温度280℃,螺杆转速50rpm/min,输出压力为15Mpa,冷却辊温度60℃,双向拉伸倍率为8×10倍,定型温度120℃,定型时间1min,产品性能见表1。
表1
由表1可以看出,以TPX为原料所制备的微孔膜,其机械强度、热稳定性都较PE微孔膜有很大的提高,且其吸液保液性能也较PE膜好,其中TPX结晶度高,其透气性能较好。
以上是对本发明一种高强度、高热稳定性的聚(4-甲基-1戊烯)微孔膜及其制备方法进行了阐述,用于帮助理解本发明,但本发明的实施方式并不受上述实施例的限制,凡以本发明所述特征或原理做的等效修改或替换,均应包含在本发明的保护范围之内。
Claims (6)
1.一种高强度、高热稳定性的聚(4-甲基-1-戊烯)微孔膜,其特征在于,由以下组分按重量份制备而成:
聚(4-甲基-1-戊烯)树脂:25~50份;
抗氧剂:0.05~1份;
稀释剂:50~75份。
2.根据权利要求1所述的聚(4-甲基-1-戊烯)微孔膜,其特征在于,所述聚(4-甲基-1-戊烯)树脂的分子量为1×104~1×107。
3.根据权利要求1所述的聚(4-甲基-1-戊烯)微孔膜,其特征在于,所述聚(4-甲基-1-戊烯)树脂的结晶度为30-60%。
4.根据权利要求1所述的聚(4-甲基-1-戊烯)微孔膜,其特征在于,所述抗氧剂为受阻酚、抗氧剂168、抗氧剂1010、抗氧剂CA、胺类抗氧剂或有机硫化物的一种或两种以上的混合物。
5.根据权利要求1所述的聚(4-甲基-1-戊烯)微孔膜,其特征在于,所述稀释剂为十氢萘、矿物油、石蜡油中的至少一种。
6.一种制备权利要求1~7任一所述高强度、高热稳定性聚(4-甲基-1-戊烯)微孔膜的方法,其特征在于,包括如下步骤:
(1)将聚(4-甲基-1-戊烯)树脂粒料、抗氧剂及稀释剂按一定的重量比加入到挤出机,挤出机工作温度为200~350℃;挤出机螺杆转速为50~300rpm/min;输出压力为10~60MPa,塑化混炼得到混合物I;
(2)步骤(1)所述混合物I经过计量泵和过滤器过滤后输送到模头并挤出,模头温度240~400℃;然后通过冷却辊将熔体冷却制得前驱体膜,冷却辊工作温度为20~90℃;
(3)将前驱体膜进行双向拉伸,双向拉伸倍率为3~15×5~20;
(4)在室温下利用清洗剂对前驱体膜萃取除去稀释剂并干燥,所述清洗剂为醇或卤代烷烃;
(5)将步骤(4)中干燥后的膜经过热处理定型,定型温度为80~140 ℃,定型时间1~5分钟。
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