CN106380723A - 一种洗衣液凝珠的速溶膜 - Google Patents

一种洗衣液凝珠的速溶膜 Download PDF

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CN106380723A
CN106380723A CN201610748010.2A CN201610748010A CN106380723A CN 106380723 A CN106380723 A CN 106380723A CN 201610748010 A CN201610748010 A CN 201610748010A CN 106380723 A CN106380723 A CN 106380723A
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黎朝森
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Guangzhou Smosnow Health Technology Co Ltd
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Abstract

本发明涉及一种速溶膜，尤其是一种洗衣液凝珠的速溶膜，它采用淀粉基材和PVA混合后加入增溶剂、稳定剂和增塑剂混合后通过流延机成膜。通过将塑料性质的PVA与自然成分的淀粉结合，提高了速溶膜的植物成本占比，具有一定的环保效果，另外，由于淀粉材料的遇水崩解性能，大大提高了凝珠的崩解能力。

Description

一种洗衣液凝珠的速溶膜
技术领域
本发明涉及一种速溶膜，尤其是一种洗衣液凝珠的速溶膜。
背景技术
洗衣液凝珠是由速溶膜包裹的独立包装式洗衣液。现有的速溶膜一般采用PVA制成，具有易于分解等优点。但是其在常温冷水中溶解依然较慢，常常需要经过搅拌和翻滚后才能完全溶解。这就导致洗衣液不能瞬间释放，或者释放不均匀。
发明内容
针对现有技术的不足，本发明提供一种遇水快速释崩解的速溶膜。
本发明的技术方案为：
一种洗衣液凝珠的速溶膜，其特征在于：它采用淀粉基材和PVA混合后加入增溶剂、稳定剂和增塑剂混合后通过流延机成膜。
所述的淀粉基材的制作方法：取蜡质玉米羟丙基淀粉30份、经过醋酸酯化的木薯淀粉20份，过80目筛后加入常温磁化的纯化水后配制成质量浓度为30％的溶液。再加入80℃-100℃磁化的纯化水后质量浓度为15％的溶液，控制进风温度为160℃，出风温度为90℃，采用离心式雾化喷雾干燥器进行喷雾干燥，得混合粉末A；甘露醇1份，羟丙甲纤维素0.5份，山梨醇0.5份，聚维酮1份，过80目筛后混匀，磁化的纯化水后配制成质量浓度为35％的溶液。再加入80℃-100℃磁化的纯化水后质量浓度为5％的溶液，50℃真空干燥，得混合粉末B；将混合粉末A、混合粉末B按2:1比例混合均匀，充分混合均匀后减压消泡得到淀粉基材。
所述的淀粉基材的制作方法还可以是：取木薯羟丙基淀粉35份、经过醋酸酯化的木薯淀粉25份，过80目筛后过80目筛后加入常温磁化的纯化水后配制成质量浓度为30％的溶液。再加入100℃磁化的纯化水后质量浓度为15％的溶液，控制进风温度为160℃，出风温度为90℃，采用离心式雾化喷雾干燥器进行喷雾干燥，得混合粉末A；甘露醇1份，羟丙甲纤维素0.5份，山梨醇0.5份，聚维酮1份，过80目筛后混匀，磁化的纯化水后配制成质量浓度为35％的溶液。再加入100℃磁化的纯化水后质量浓度为5％的溶液，50℃真空干燥，得混合粉末B；将混合粉末A、混合粉末B按3:1比例混合均匀，充分混合均匀后减压消泡得到淀粉基材。
所述淀粉基材、PVA、增溶剂、稳定剂和增塑剂的质量百分比为：
50％-60％，40％-50％，0.1％-1％，0.1％-1％，9％-10％。
进一步地，所述淀粉基材、PVA、增溶剂、稳定剂和增塑剂的质量百分比为：
50％，40％，0.5％，0.5％，9％。
进一步地，所述混合中温度保持在60-80摄氏度。
进一步地，所述流延机成膜过程为：分布、预热、成膜、烘干和卷膜。
本发明的有益效果为：本发明通过将塑料性质的PVA与自然成分的淀粉结合，提高了速溶膜的植物成本占比，具有一定的环保效果，另外，由于淀粉材料的遇水崩解性能，大大提高了凝珠的崩解能力。
具体实施方式
下面结合实施例对本发明的具体实施方式作进一步说明：
实施例1
取蜡质玉米羟丙基淀粉30份、经过醋酸酯化的木薯淀粉20份，过80目筛后加入常温磁化的纯化水后配制成质量浓度为30％的溶液。再加入80℃-100℃磁化的纯化水后质量浓度为15％的溶液，控制进风温度为160℃，出风温度为90℃，采用离心式雾化喷雾干燥器进行喷雾干燥，得混合粉末A；甘露醇1份，羟丙甲纤维素0.5份，山梨醇0.5份，聚维酮1份，过80目筛后混匀，磁化的纯化水后配制成质量浓度为35％的溶液。再加入80℃-100℃磁化的纯化水后质量浓度为5％的溶液，50℃真空干燥，得混合粉末B；将混合粉末A、混合粉末B按2:1比例混合均匀，充分混合均匀后减压消泡得到淀粉基材。
采用淀粉基材和PVA混合后加入增溶剂、稳定剂和增塑剂混合后通过流延机成膜。
所述淀粉基材、PVA、增溶剂、稳定剂和增塑剂的质量百分比为：
50％，40％，0.5％，0.5％，9％。
所述混合中温度保持在60-80摄氏度。所述流延机成膜过程为：分布、预热、成膜、烘干和卷膜。
实施例2
取木薯羟丙基淀粉35份、经过醋酸酯化的木薯淀粉25份，过80目筛后过80目筛后加入常温磁化的纯化水后配制成质量浓度为30％的溶液。再加入100℃磁化的纯化水后质量浓度为15％的溶液，控制进风温度为160℃，出风温度为90℃，采用离心式雾化喷雾干燥器进行喷雾干燥，得混合粉末A；甘露醇1份，羟丙甲纤维素0.5份，山梨醇0.5份，聚维酮1份，过80目筛后混匀，磁化的纯化水后配制成质量浓度为35％的溶液。再加入100℃磁化的纯化水后质量浓度为5％的溶液，50℃真空干燥，得混合粉末B；将混合粉末A、混合粉末B按3:1比例混合均匀，充分混合均匀后减压消泡得到淀粉基材。
采用淀粉基材和PVA混合后加入增溶剂、稳定剂和增塑剂混合后通过流延机成膜。
所述淀粉基材、PVA、增溶剂、稳定剂和增塑剂的质量百分比为：
50％，40％，0.5％，0.5％，9％。
所述混合中温度保持在60-80摄氏度。所述流延机成膜过程为：分布、预热、成膜、烘干和卷膜。
上述实施例和说明书中描述的只是说明本发明的原理和最佳实施例，在不脱离本发明精神和范围的前提下，本发明还会有各种变化和改进，这些变化和改进都落入要求保护的本发明范围内。

Claims (7)

1.一种洗衣液凝珠的速溶膜，其特征在于：它采用淀粉基材和PVA混合后加入增溶剂、稳定剂和增塑剂混合后通过流延机成膜。
2.根据权利要求1所述的洗衣液凝珠的速溶膜，其特征在于：所述的淀粉基材的制作方法：取蜡质玉米羟丙基淀粉30份、经过醋酸酯化的木薯淀粉20份，过80目筛后加入常温磁化的纯化水后配制成质量浓度为30％的溶液。再加入80℃-100℃磁化的纯化水后质量浓度为15％的溶液，控制进风温度为160℃，出风温度为90℃，采用离心式雾化喷雾干燥器进行喷雾干燥，得混合粉末A；甘露醇1份，羟丙甲纤维素0.5份，山梨醇0.5份，聚维酮1份，过80目筛后混匀，磁化的纯化水后配制成质量浓度为35％的溶液。再加入80℃-100℃磁化的纯化水后质量浓度为5％的溶液，50℃真空干燥，得混合粉末B；将混合粉末A、混合粉末B按2:1比例混合均匀，充分混合均匀后减压消泡得到淀粉基材。
3.根据权利要求2所述的洗衣液凝珠的速溶膜，其特征在于：所述的淀粉基材的制作方法还可以是：取木薯羟丙基淀粉35份、经过醋酸酯化的木薯淀粉25份，过80目筛后过80目筛后加入常温磁化的纯化水后配制成质量浓度为30％的溶液。再加入100℃磁化的纯化水后质量浓度为15％的溶液，控制进风温度为160℃，出风温度为90℃，采用离心式雾化喷雾干燥器进行喷雾干燥，得混合粉末A；甘露醇1份，羟丙甲纤维素0.5份，山梨醇0.5份，聚维酮1份，过80目筛后混匀，磁化的纯化水后配制成质量浓度为35％的溶液。再加入100℃磁化的纯化水后质量浓度为5％的溶液，50℃真空干燥，得混合粉末B；将混合粉末A、混合粉末B按3:1比例混合均匀，充分混合均匀后减压消泡得到淀粉基材。
4.根据权利要求3所述的洗衣液凝珠的速溶膜，其特征在于：所述淀粉基材、PVA、增溶剂、稳定剂和增塑剂的质量百分比为：50％-60％，40％-50％，0.1％-1％，0.1％-1％，9％-10％。
5.根据权利要求4所述的洗衣液凝珠的速溶膜，其特征在于：所述淀粉基材、PVA、增溶剂、稳定剂和增塑剂的质量百分比为：50％，40％，0.5％，0.5％，9％。
6.根据权利要求5所述的洗衣液凝珠的速溶膜，其特征在于：所述混合中温度保持在60-80摄氏度。
7.根据权利要求6所述的洗衣液凝珠的速溶膜，其特征在于：所述流延机成膜过程为：分布、预热、成膜、烘干和卷膜。
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Citations (1)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
CN1363628A (zh) * 2002-01-16 2002-08-14 郝喜海 调控水溶性薄膜的水溶解速度的方法

Patent Citations (1)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
CN1363628A (zh) * 2002-01-16 2002-08-14 郝喜海 调控水溶性薄膜的水溶解速度的方法

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