CN112109340A - 一种利用回收的废旧pet塑料制备编织袋的工艺 - Google Patents
一种利用回收的废旧pet塑料制备编织袋的工艺 Download PDFInfo
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Abstract
一种利用回收的废旧PET塑料制备编织袋的工艺,其步骤为:(1)回收品清洗;(2)原料配方;(3)共混前料准备;(4)共混;(5)拉丝;(6)织布;(7)切袋;(8)印刷。本发明通过单螺杆、双螺杆加上采用熔体定压计量技术直接进行拉丝操作,使废旧原料和最终产品一体化,可以大大降低加工能耗,解决了废旧PET瓶片的节能脱水技术和复合材料的拉丝技术,由于PET和PP的溶点不一致,因此单丝拉伸取向温度不一致,直接拉丝和单丝取向的技术问题。
Description
技术领域
本发明涉及编织袋领域,尤其涉及一种利用回收的废旧PET塑料制备编织袋的工艺。
背景技术
PET为聚对苯二甲酸二醇酯,PET的韧性极佳,其薄膜的拉伸强度比PC的高出三倍,比PE高出九倍,可以与铝膜相比美,而且比其它塑料膜的冲击强度高出四倍多,且具有长期耐热氧老化性能,饮料瓶、矿泉水瓶等包装瓶用PET己经成为回收再利用的主要方向,塑编行业产量巨大,废旧PET的应用空间很大,但纯回收PET的扁丝拉丝难度较大,如果可以将废旧PET应用到塑料编织袋的生产中,对生态的可持续发展将具有长远而重要意义。
发明内容
本发明为实现废旧PET作为原料用于制备编织袋中提供了一种制备工艺,利用废旧PET塑料与PP和PE共混从而达到编织袋所要求的强度。
本发明所采取的技术方案:
一种利用回收的废旧PET塑料制备编织袋的工艺,其步骤为:
(1)回收品清洗:回收的PET废旧塑料、废旧编织袋、废旧PP薄膜/
清洗,烘干;
(2)原料配方:废旧PET:25-40份、废旧PP:55-65份、回收HDPE:5-10份、相容剂:8-12份、抗氧剂0.3-0.4份、填充剂CaCO3母粒25-35份、扩链剂:0.5-2.5份;
(3)共混前料准备:将回收的PP、相容剂、抗氧剂和填充剂按配方比例加入到高速混合机中,高速混合1-2min后出料,将混合物加入到单螺杆挤出机中熔融混炼;将废旧PET塑料、扩链剂、抗氧剂按配方比例加入到高速混合机中,高速混合2-3min,加热到150~160℃,密闭输送到另一台双螺杆挤出机中增粘;
(4)共混:单螺杆挤出机和双螺杆挤出机挤出的熔体直接加入到第三台双螺杆挤出机中进行共混,通过熔体计量泵和T型机头挤出;
(5)拉丝:螺杆挤出机熔融,用平膜法以薄膜形式挤出并水冷,切刀将薄膜纵向切割成坯丝,坯丝经过烘箱被拉伸为扁丝,扁丝通过热定型和牵伸取向后在卷绕机上收卷成型;
(6)织布:将扁丝分为经线和纬线,将经线通过送经倒辊和跳杆上下交替的棕丝,使经线间形成开口、闭合、反向开口、闭合,即经线开交,同时,纬线随梭子和经线开口沿水平做圆周运动,将经纬线编制成织布并将织布收卷;
(7)切袋:对织布进行电晕处理,然后将电晕好的织布进行切袋;
(8)印刷:对编织袋内表面进行印刷。
所述的相容剂为HDPE-g-MAH、LLDPE-g-MAH、LDPE-G-MAH和PP-g-MAH中的一种或多种。
所述的抗氧剂为抗氧剂1010和抗氧剂168。
所述的扩链剂为环氧树脂SAG-008和均苯四甲酸二酐。
所述的回收PP单螺杆挤出机参数为一区200℃、二区210℃、三区220℃、四区230℃、五区240℃、六区245℃,机头温度238℃,主机转速230/rpm。
所述的回收PET双螺杆挤出机参数为一区182℃、二区213℃、三区242℃、四区232℃、五区226℃、六区233℃、七区231℃、八区206℃,熔体温度206℃,机头温度206℃,喂料速度16.4r/min,主机转速178/rpm。
所述的回收PET和回收PP共混挤出机参数为一区153℃、二区163℃、三区238℃、四区220℃、五区221℃、六区220℃、七区211℃、八区211℃、九区214℃,熔体温度220℃,机头温度218℃,喂料速度28.2r/min,主机转速268/rpm。
本发明的有益效果:本发明通过单螺杆、双螺杆加上采用熔体定压计量技术直接进行拉丝操作,使废旧原料和最终产品一体化,可以大大降低加工能耗,解决了废旧PET瓶片的节能脱水技术和复合材料的拉丝技术,由于PET和PP的溶点不一致,因此单丝拉伸取向温度不一致,直接拉丝和单丝取向的技术问题。
具体实施方式
一种利用回收的废旧PET塑料制备编织袋的工艺,其步骤为:
(1)回收品清洗:回收的PET废旧塑料、废旧编织袋、废旧PP薄膜/
清洗,烘干;
(2)原料配方:废旧PET:25-40份、废旧PP:55-65份、回收HDPE:5-10份、相容剂:8-12份、抗氧剂0.3-0.4份、填充剂CaCO3母粒25-35份、扩链剂:0.5-2.5份;相容剂为HDPE-g-MAH、LLDPE-g-MAH、LDPE-G-MAH和PP-g-MAH中的一种或多种,抗氧剂为抗氧剂1010和抗氧剂168,扩链剂为环氧树脂SAG-008和均苯四甲酸二酐。
(3)共混前料准备:将回收的PP、相容剂、抗氧剂和填充剂按配方比例加入到高速混合机中,高速混合1-2min后出料,将混合物加入到单螺杆挤出机中熔融混炼,单螺杆挤出机参数为一区200℃、二区210℃、三区220℃、四区230℃、五区240℃、六区245℃,机头温度238℃,主机转速230/rpm;将废旧PET塑料、扩链剂、抗氧剂按配方比例加入到高速混合机中,高速混合2-3min,加热到150~160℃,密闭输送到另一台双螺杆挤出机中增粘,双螺杆挤出机参数为一区182℃、二区213℃、三区242℃、四区232℃、五区226℃、六区233℃、七区231℃、八区206℃,熔体温度206℃,机头温度206℃,喂料速度16.4r/min,主机转速178/rpm;
(4)共混:单螺杆挤出机和双螺杆挤出机挤出的熔体直接加入到第三台双螺杆挤出机中进行共混,通过熔体计量泵和T型机头挤出,共混挤出机参数为一区153℃、二区163℃、三区238℃、四区220℃、五区221℃、六区220℃、七区211℃、八区211℃、九区214℃,熔体温度220℃,机头温度218℃,喂料速度28.2r/min,主机转速268/rpm;
(5)拉丝:螺杆挤出机熔融,用平膜法以薄膜形式挤出并水冷,切刀将薄膜纵向切割成坯丝,坯丝经过烘箱被拉伸为扁丝,扁丝通过热定型和牵伸取向后在卷绕机上收卷成型;
(6)织布:将扁丝分为经线和纬线,将经线通过送经倒辊和跳杆上下交替的棕丝,使经线间形成开口、闭合、反向开口、闭合,即经线开交,同时,纬线随梭子和经线开口沿水平做圆周运动,将经纬线编制成织布并将织布收卷;
(7)切袋:对织布进行电晕处理,然后将电晕好的织布进行切袋;
(8)印刷:对编织袋内表面进行印刷。
下面将结合具体实施例对本发明进行详细阐述:
一种利用回收的废旧PET塑料制备编织袋的工艺,其步骤为:
(1)回收品清洗:回收的PET废旧塑料、废旧编织袋、废旧PP薄膜/
清洗,烘干;
(2)原料配方:废旧PET:35份、废旧PP:55份、回收HDPE:10份、相容剂:8份、抗氧剂0.34份、填充剂CaCO3母粒30份、扩链剂:2份;相容剂为HDPE-g-MAH、LLDPE-g-MAH、LDPE-G-MAH和PP-g-MAH中的一种或多种,抗氧剂为抗氧剂1010和抗氧剂168,扩链剂为环氧树脂SAG-008和均苯四甲酸二酐。
(3)共混前料准备:将回收的PP、相容剂、抗氧剂和填充剂按配方比例加入到高速混合机中,高速混合2min后出料,将混合物加入到单螺杆挤出机中熔融混炼,单螺杆挤出机参数为一区200℃、二区210℃、三区220℃、四区230℃、五区240℃、六区245℃,机头温度238℃,主机转速230/rpm;将废旧PET塑料、扩链剂、抗氧剂按配方比例加入到高速混合机中,高速混合3min,加热到155℃,密闭输送到另一台双螺杆挤出机中增粘,双螺杆挤出机参数为一区182℃、二区213℃、三区242℃、四区232℃、五区226℃、六区233℃、七区231℃、八区206℃,熔体温度206℃,机头温度206℃,喂料速度16.4r/min,主机转速178rpm;
(4)共混:单螺杆挤出机和双螺杆挤出机挤出的熔体直接加入到第三台双螺杆挤出机中进行共混,通过熔体计量泵和T型机头挤出,共混挤出机参数为一区153℃、二区163℃、三区238℃、四区220℃、五区221℃、六区220℃、七区211℃、八区211℃、九区214℃,熔体温度220℃,机头温度218℃,喂料速度28.2r/min,主机转速268rpm;
(5)拉丝:螺杆挤出机熔融,用平膜法以薄膜形式挤出并水冷,切刀将薄膜纵向切割成坯丝,坯丝经过烘箱被拉伸为扁丝,扁丝通过热定型和牵伸取向后在卷绕机上收卷成型;
(6)织布:将扁丝分为经线和纬线,将经线通过送经倒辊和跳杆上下交替的棕丝,使经线间形成开口、闭合、反向开口、闭合,即经线开交,同时,纬线随梭子和经线开口沿水平做圆周运动,将经纬线编制成织布并将织布收卷;
(7)切袋:对织布进行电晕处理,然后将电晕好的织布进行切袋;
(8)印刷:对编织袋内表面进行印刷。
以上对本发明的实施例进行了详细说明,但所述内容仅为本发明的较佳实施例,不能被认为用于限定本发明的实施范围。凡依本发明申请范围所作的均等变化与改进等,均应仍归属于本发明的专利涵盖范围之内。
Claims (7)
1.一种利用回收的废旧PET塑料制备编织袋的工艺,其特征在于,其步骤为:
(1)回收品清洗:回收的PET废旧塑料、废旧编织袋、废旧PP薄膜/清洗,烘干;
(2)原料配方:废旧PET:25-40份、废旧PP:55-65份、回收HDPE:5-10份、相容剂:8-12份、抗氧剂0.3-0.4份、填充剂CaCO3母粒25-35份、扩链剂:0.5-2.5份;
(3)共混前料准备:将回收的PP、相容剂、抗氧剂和填充剂按配方比例加入到高速混合机中,高速混合1-2min后出料,将混合物加入到单螺杆挤出机中熔融混炼;将废旧PET塑料、扩链剂、抗氧剂按配方比例加入到高速混合机中,高速混合2-3min,加热到150~160℃,密闭输送到另一台双螺杆挤出机中增粘;
(4)共混:单螺杆挤出机和双螺杆挤出机挤出的熔体直接加入到第三台双螺杆挤出机中进行共混,通过熔体计量泵和T型机头挤出;
(5)拉丝:螺杆挤出机熔融,用平膜法以薄膜形式挤出并水冷,切刀将薄膜纵向切割成坯丝,坯丝经过烘箱被拉伸为扁丝,扁丝通过热定型和牵伸取向后在卷绕机上收卷成型;
(6)织布:将扁丝分为经线和纬线,将经线通过送经倒辊和跳杆上下交替的棕丝,使经线间形成开口、闭合、反向开口、闭合,即经线开交,同时,纬线随梭子和经线开口沿水平做圆周运动,将经纬线编制成织布并将织布收卷;
(7)切袋:对织布进行电晕处理,然后将电晕好的织布进行切袋;
(8)印刷:对编织袋内表面进行印刷。
2.根据权利要求1所述的利用回收的废旧PET塑料制备编织袋的工艺,其特征在于,所述的相容剂为HDPE-g-MAH、LLDPE-g-MAH、LDPE-G-MAH和PP-g-MAH中的一种或多种。
3.根据权利要求1所述的利用回收的废旧PET塑料制备编织袋的工艺,其特征在于,所述的抗氧剂为抗氧剂1010和抗氧剂168。
4.根据权利要求1所述的利用回收的废旧PET塑料制备编织袋的工艺,其特征在于,所述的扩链剂为环氧树脂SAG-008和均苯四甲酸二酐。
5.根据权利要求1所述的利用回收的废旧PET塑料制备编织袋的工艺,其特征在于,所述的回收PP单螺杆挤出机参数为一区200℃、二区210℃、三区220℃、四区230℃、五区240℃、六区245℃,机头温度238℃,主机转速230/rpm。
6.根据权利要求1所述的利用回收的废旧PET塑料制备编织袋的工艺,其特征在于,所述的回收PET双螺杆挤出机参数为一区182℃、二区213℃、三区242℃、四区232℃、五区226℃、六区233℃、七区231℃、八区206℃,熔体温度206℃,机头温度206℃,喂料速度16.4r/min,主机转速178rpm。
7.根据权利要求1所述的利用回收的废旧PET塑料制备编织袋的工艺,其特征在于,所述的回收PET和回收PP共混挤出机参数为一区153℃、二区163℃、三区238℃、四区220℃、五区221℃、六区220℃、七区211℃、八区211℃、九区214℃,熔体温度220℃,机头温度218℃,喂料速度28.2r/min,主机转速268rpm。
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