CN113212921B - 一种可降解塑料瓶及其制备方法 - Google Patents
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Abstract
一种可降解塑料瓶及其制备方法,它涉及塑料材料技术领域。它包含以下步骤方法:步骤一,按相应重量比例称取各成分的含量;步骤二,将称重后的组份进行粉碎加工;步骤三,将粉碎后的组份进行筛选处理;步骤四,将筛选后的组份采用高速混合机进行充分混合;步骤五,将混合后的组份进行造粒加工;步骤六,将形成的可降解塑料通过挤塑机挤出成型。该制备方法制成的可降解塑料瓶具有一定的可降解性,使用时具有一定的抗冲击性、耐腐蚀和抗氧化,废气后在段时间内可被环境消纳,大大缓解了对环境的污染,不会对人体身心健康造成损害,该方法制备形成的塑料瓶具有一定的市场推广价值。
Description
技术领域
本发明涉及塑料材料技术领域,具体涉及一种可降解塑料瓶及其制备方法。
背景技术
塑料瓶具有强度高、质量轻、抗腐蚀、价格便宜等特点,在人们的生产生活中得到广泛应用。塑料瓶的应用在给人们带来极大方便的同时也带来严重的负面影响,大部分废弃的塑料瓶除了可在特殊条件下降解外,其在自然界环境中的光、生物降解速度非常缓慢,大概需要几百年的时间才可能完全消失,虽然其可通过掩埋、焚烧等方法来处理,但这些方法存在极大的缺陷。大量使用后的废弃塑料无法自动降解,长期残留在自然环境中可造成严重的环境污染,不仅影响生态平衡,同时也威胁着人类的健康。据不完全统计,全球每年生产的塑料瓶超过亿吨,而我国的塑料瓶占了相当大的比例,其中一次性塑料制品较多。使用后废弃的塑料瓶具有数量大、分布广、难回收等特点,形成白色垃圾,造成严重的环境污染。
为了解决这一问题,可降解塑料成为研究者们关注的热点,虽然可降解塑料的研究取得了一定成果,但可降解塑料仍然存在降解不充分等缺陷缺陷,使其应用范围受到了限制。
发明内容
本发明的目的在于针对现有技术的缺陷和不足,提供一种可降解塑料瓶及其制备方法,以解决上述背景技术中提出的问题,本发明具有一定的可降解性,使用时具有一定的抗冲击性、耐腐蚀和抗氧化,废气后在段时间内可被环境消纳,大大缓解了对环境的污染,不会对人体身心健康造成损害,该方法制备形成的塑料瓶具有一定的市场推广价值。
为实现上述目的,本发明采用以下技术方案是:它包含塑料瓶本体1、瓶盖2,所述的塑料瓶本体1顶部设置有瓶盖2且两者之间通过螺纹齿合活动连接,所述的塑料瓶本体1的底部设置有底座11,顶部设置有瓶口12,所述的塑料瓶本体1靠近底座11处设置有下弧形部13,所述的塑料瓶本体1靠近瓶口12处设置有上弧形部14,所述的底座11上等间距设置有第一加强筋15,所述的下弧形部13上等间距设置有第二加强筋16,所述的上弧形部14上等间距设置有第三加强筋17,所述的瓶口12下部与塑料瓶本体1的连接部设置有固定环18,所述的固定环18上设置有密封圈19,所述的密封圈19上安装有支撑垫20,所述的瓶盖2设置在支撑垫20的上方,所述的瓶盖2内壁设置有内螺纹,所述的瓶口12的外周设置有外螺纹,所述的瓶盖2与瓶口12通过螺纹齿合连接固定。
所述的一种可降解塑料瓶包含以下重量份数的组份:聚氯乙烯醇30-50份、聚已内酯10-20份、聚乳酸2-5份、脂肪族芳香族共聚酯2-5份、改性淀粉5-10份、纤维素2-5份、甲壳质2-3份、光敏剂20-30份,所述的光敏剂为抗氧剂1010或抗氧剂264中的一种或两种。
所述的一种可降解塑料瓶包含以下步骤方法:步骤一,按相应重量比例称取各成分的含量;步骤二,将称重后的组份进行粉碎加工;步骤三,将粉碎后的组份进行筛选处理;步骤四,将筛选后的组份采用高速混合机进行充分混合;步骤五,将混合后的组份进行造粒加工;步骤六,将形成的可降解塑料通过挤塑机挤出成型。
所述的步骤二中粉碎的目数大小为60-120目,目数大小太粗了会造成表面粗糙,手感不好,容易站脏,太细了又不经济,目数大小在粉碎过程中尤为重要。
所述的步骤三中特别是改性淀粉筛选尤为重要,颗粒较大在压延过程中高温高压下水分汽化容易产生针眼,成型后容易出现大孔,导致成品报废。
所述的步骤四中混合过程需增设预热装置与抽湿装置,因在混合过程中靠之间组份的磨擦发热效率较低,温控幅度较窄,温度的把控对成品率有一定影响,所以需要增加预热装置,针对改性淀粉混合时最重要的是控制水分,若改性淀粉一点水分都没有,塑化效果不好,水分过多的话粒料会产生气泡,混合温度一般控制在90-115℃,时间为30-150min。
所述的步骤五中造粒过程采用双螺杆挤出机,所述的双螺杆挤出机包含挤入过程、第一挤压过程、第二挤压过程、挤出过程,所述的挤入过程温度为140-170℃,第一挤压过程温度为190-200℃,第二挤压过程温度为210-220℃,挤出过程温度为105-130℃。
所述的步骤六中挤塑机温度分为八段,一段160-165℃,二段160-170℃,三段165-170℃,四段160-170℃,五段160-170℃,六段165-170℃,七段165-170℃,八段165-170℃,每端挤压时间为0.5-1s,吹气时间为2-2.5s,排气时间为1-1.5s,动作压力为0.1-1MPa,吹气压力为0.4-0.8MPa。
采用上述技术方案后,本发明有益效果为:具有一定的可降解性,使用时具有一定的抗冲击性、耐腐蚀和抗氧化,废弃后在段时间内可被环境消纳,大大缓解了对环境的污染,不会对人体身心健康造成损害,该方法制备形成的塑料瓶具有一定的市场推广价值。
附图说明
为了更清楚地说明本发明实施例或现有技术中的技术方案,下面将对实施例或现有技术描述中所需要使用的附图作简单地介绍,显而易见地,下面描述中的附图仅仅是本发明的一些实施例,对于本领域普通技术人员来讲,在不付出创造性劳动性的前提下,还可以根据这些附图获得其他的附图。
图1是本发明的结构示意图;
图2是对应图1的俯视结构示意图。
附图标记说明:塑料瓶本体1、底座11、瓶口12、下弧形部13、上弧形部14、第一加强筋15、第二加强筋16、第三加强筋17、固定环18、密封圈19、支撑垫20、瓶盖2。
具体实施方式
参看图1-图2所示,本具体实施方式采用的技术方案是:它包含塑料瓶本体1、瓶盖2,所述的塑料瓶本体1顶部设置有瓶盖2且两者之间通过螺纹齿合活动连接,所述的塑料瓶本体1的底部设置有底座11,顶部设置有瓶口12,所述的塑料瓶本体1靠近底座11处设置有下弧形部13,所述的塑料瓶本体1靠近瓶口12处设置有上弧形部14,所述的底座11上等间距设置有第一加强筋15,所述的下弧形部13上等间距设置有第二加强筋16,所述的上弧形部14上等间距设置有第三加强筋17,所述的瓶口12下部与塑料瓶本体1的连接部设置有固定环18,所述的固定环18上设置有密封圈19,所述的密封圈19上安装有支撑垫20,所述的瓶盖2设置在支撑垫20的上方,所述的瓶盖2内壁设置有内螺纹,所述的瓶口12的外周设置有外螺纹,所述的瓶盖2与瓶口12通过螺纹齿合连接固定。
进一步的,所述的一种可降解塑料瓶包含以下重量份数的组份:聚氯乙烯醇30-50份、聚已内酯10-20份、聚乳酸2-5份、脂肪族芳香族共聚酯2-5份、改性淀粉5-10份、纤维素2-5份、甲壳质2-3份、光敏剂20-30份,所述的光敏剂为抗氧剂1010或抗氧剂264中的一种或两种。
进一步的,所述的一种可降解塑料瓶包含以下步骤方法:步骤一,按相应重量比例称取各成分的含量;步骤二,将称重后的组份进行粉碎加工;步骤三,将粉碎后的组份进行筛选处理;步骤四,将筛选后的组份采用高速混合机进行充分混合;步骤五,将混合后的组份进行造粒加工;步骤六,将形成的可降解塑料通过挤塑机挤出成型。
进一步的,所述的步骤二中粉碎的目数大小为60-120目,目数大小太粗了会造成表面粗糙,手感不好,容易站脏,太细了又不经济,目数大小在粉碎过程中尤为重要。
进一步的,所述的步骤三中特别是改性淀粉筛选尤为重要,颗粒较大在压延过程中高温高压下水分汽化容易产生针眼,成型后容易出现大孔,导致成品报废。
进一步的,所述的步骤四中混合过程需增设预热装置与抽湿装置,因在混合过程中靠之间组份的磨擦发热效率较低,温控幅度较窄,温度的把控对成品率有一定影响,所以需要增加预热装置,针对改性淀粉混合时最重要的是控制水分,若改性淀粉一点水分都没有,塑化效果不好,水分过多的话粒料会产生气泡,混合温度一般控制在90-115℃,时间为30-150min。
进一步的,所述的步骤五中造粒过程采用双螺杆挤出机,所述的双螺杆挤出机包含挤入过程、第一挤压过程、第二挤压过程、挤出过程,所述的挤入过程温度为140-170℃,当挤入过程温度太低时,双螺杆挤出机的背压太大,塑化也不好,原料在出口处不能成直流状,而成为翻卷的面片状,第一挤压过程温度为190-200℃,原料在出口处有较多的气泡产生,颜色变黄,第二挤压过程温度为210-220℃,原料在出口处呈棕色膨化状,挤出过程温度为105-130℃,流道要光洁、无死角、要有控温,温差小。
进一步的,所述的步骤六中挤塑机温度分为八段,一段160-165℃,二段160-170℃,三段165-170℃,四段160-170℃,五段160-170℃,六段165-170℃,七段165-170℃,八段165-170℃,每端挤压时间为0.5-1s,吹气时间为2-2.5s,排气时间为1-1.5s,动作压力为0.1-1MPa,吹气压力为0.4-0.8MPa。
采用上述技术方案后,本发明有益效果为:具有一定的可降解性,使用时具有一定的抗冲击性、耐腐蚀和抗氧化,废气后在段时间内可被环境消纳,大大缓解了对环境的污染,不会对人体身心健康造成损害,该方法制备形成的塑料瓶具有一定的市场推广价值。
以上所述,仅用以说明本发明的技术方案而非限制,本领域普通技术人员对本发明的技术方案所做的其它修改或者等同替换,只要不脱离本发明技术方案的精神和范围,均应涵盖在本发明的权利要求范围当中。
Claims (1)
1.一种可降解塑料瓶,其特征在于:它包含塑料瓶本体(1)、瓶盖(2),所述的塑料瓶本体(1)顶部设置有瓶盖(2)且两者之间通过螺纹齿合活动连接,所述的塑料瓶本体(1)的底部设置有底座(11),顶部设置有瓶口(12),所述的塑料瓶本体(1)靠近底座(11)处设置有下弧形部(13),所述的塑料瓶本体(1)靠近瓶口(12)处设置有上弧形部(14),所述的底座(11)上等间距设置有第一加强筋(15),所述的下弧形部(13)上等间距设置有第二加强筋(16),所述的上弧形部(14)上等间距设置有第三加强筋(17),所述的瓶口(12)下部与塑料瓶本体(1)的连接部设置有固定环(18),所述的固定环(18)上设置有密封圈(19),所述的密封圈(19)上安装有支撑垫(20),所述的瓶盖(2)设置在支撑垫(20)的上方,所述的瓶盖(2)内壁设置有内螺纹,所述的瓶口(12)的外周设置有外螺纹,所述的瓶盖(2)与瓶口(12)通过螺纹齿合连接固定;
可降解塑料瓶的制备方法,包含以下重量份数的组份:聚氯乙烯醇30-50份、聚已内酯10-20份、聚乳酸2-5份、脂肪族芳香族共聚酯2-5份、改性淀粉5-10份、纤维素2-5份、甲壳质2-3份、光敏剂20-30份,所述的光敏剂为抗氧剂1010或抗氧剂264中的一种或两种;
其中,步骤一,按相应重量比例称取各成分的含量;步骤二,将称重后的组份进行粉碎加工;步骤三,将粉碎后的组份进行筛选处理;步骤四,将筛选后的组份采用高速混合机进行充分混合;步骤五,将混合后的组份进行造粒加工;步骤六,将形成的可降解塑料通过挤塑机挤出成型;所述的步骤二中粉碎的目数大小为60-120目;所述的步骤四中混合过程需增设预热装置与抽湿装置,混合温度一般控制在90-115℃,时间为30-150min;所述的步骤五中造粒过程采用双螺杆挤出机,所述的双螺杆挤出机包含挤入过程、第一挤压过程、第二挤压过程、挤出过程,所述的挤入过程温度为140-170℃,第一挤压过程温度为190-200℃,第二挤压过程温度为210-220℃,挤出过程温度为105-130℃;所述的步骤六中挤塑机温度分为八段,一段160-165℃,二段160-170℃,三段165-170℃,四段160-170℃,五段160-170℃,六段165-170℃,七段165-170℃,八段165-170℃,每段挤压时间为0.5-1s,吹气时间为2-2.5s,排气时间为1-1.5s,动作压力为0.1-1MPa,吹气压力为0.4-0.8MPa。
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