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CN112760076A - 一种无溶剂双组份铝塑蒸煮胶及其制备方法 - Google Patents

一种无溶剂双组份铝塑蒸煮胶及其制备方法 Download PDF

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CN112760076A
CN112760076A CN202011604567.1A CN202011604567A CN112760076A CN 112760076 A CN112760076 A CN 112760076A CN 202011604567 A CN202011604567 A CN 202011604567A CN 112760076 A CN112760076 A CN 112760076A
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蔡栋宇
蔡炳照
顾嘉卫
周锦君
项尚林
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Abstract

本发明公开了一种耐高温的无溶剂双组份聚氨酯胶粘剂,通过引进高官能团聚醚和合成合适的聚酯多元醇,提高胶水的耐温性及抗介质性能,同时解决了铝塑外层难题,这种无溶剂双组份铝塑蒸煮胶粘剂是由A胶和B胶组成,A胶是由聚酯多元醇、液化MDI和聚醚多元醇反应而成,B胶是由含有高官能团聚醚多元醇、偶联剂和蓖麻油组成,A胶和B胶配比为100:45。

Description

一种无溶剂双组份铝塑蒸煮胶及其制备方法
技术领域:
本发明涉及一种无溶剂双组份铝塑蒸煮胶及其制备方法。
背景技术:
无溶剂复合胶水由于其明显的环保性、安全性及成本优势,在国内外得到 了迅速发展和应用。随着无溶剂技术的不断提高,普通的无溶剂胶水,已经不 能满足市场需求。使用普通胶水,外层复合任需使用溶剂型聚氨酯粘合剂,产 品的环保性、安全性大打折扣。
发明内容:
本发明的目的是提供一种耐高温的无溶剂双组份聚氨酯胶粘剂,通过引进高官能团聚醚和合成合适的聚酯多元醇,提高胶水的耐温性及抗介质性能,同时解决了铝塑外层难题。
一种无溶剂双组份铝塑蒸煮胶粘剂是由A胶和B胶组成,其特征在于:A胶是由聚酯多元醇、液化MDI和聚醚多元醇反应而成,B胶是由含有高官能团聚醚多元醇、偶联剂和蓖麻油组成,A胶和B胶配比为100:45。
在所述无溶剂双组份铝塑蒸煮胶中,所述的聚酯多元醇是由含有小分子二元酸与二元醇缩聚而成。
在所述无溶剂双组份铝塑蒸煮胶中,所述的小分子二元酸为己二酸、间苯二甲酸、癸二酸、对苯二甲酸、邻苯二甲酸酐中的一种或两种的混合物。优选间苯二甲酸、己二酸或癸二酸,所述的二元醇为乙二醇、二乙二醇、新戊二醇、 1,2丙二醇,甲基丙二醇、甘油、环己烷二甲醇、1,4-丁二醇、1,6-己二醇中的一种或两种的混合物。优选环己烷二甲醇和1,6-己二醇。
在所述无溶剂双组份铝塑蒸煮胶中,所述的聚醚多元醇为:平均分子量 1000的聚氧化丙烯二醇,分子量400~2000的聚氧化丙烯四醇或分子量400~500 的聚氧化丙烯五醇。
在所述无溶剂双组份铝塑蒸煮胶中,所述的硅烷偶联剂为:γ―氨丙基三乙氧基硅烷、γ―氨丙基三甲氧基硅烷、N-(2-氨乙基)-3-氨丙基三甲氧基硅烷、 N-(2-氨乙基)-3-氨丙基三乙氧基硅烷、苯胺甲基三乙氧基硅烷、3-甲基丙烯酰氧丙基三甲氧基硅烷中的一种或两种以上的混合物。
所述无溶剂双组份铝塑蒸煮胶的制备方法如下:
(1)聚酯多元醇的制备:
在带有温度计、搅拌器、球式冷却器、氮气密封管的四口烧瓶中,加入间苯二甲酸120.6g,己二酸318.1g,葵二酸146.8g,环乙烷二甲醇704.7g,1.6- 己二醇352.4g和0.2~0.25g钛酸四丁酯催化剂,搅拌均匀,然后缓慢升温,在160℃~230℃下反应14小时后,取样测酸价,若酸价小于20mgKOH/g,则酯化合格,酯化合格后进行缩聚反应,在温度220~230℃条件下,在-0.1Mpa下抽真空5小时,得到酸价≤1mgKOH/g,羟值112±5mgKOH/g的聚酯多元醇。
(2)A胶的制备
将上述酯化缩聚后得到的聚酯多元醇100g,分子量1000聚氧化丙烯二醇及 100g,在120℃条件下真空脱水2小时,至体系含水量少于0.05%,降温至40 ℃,加入4,4-二苯基甲烷二异氰酸酯(MDI)228.6g与251.6g反应,,温度控制在80℃±5℃,反应5小时,得粘度在5000~6000mPa.s/25℃,NCO=14~15%的主胶。
B胶的制备:
取分子量400~2000的聚氧化丙烯四醇或分子量400~500的聚氧化丙烯五醇300g,蓖麻油500g和偶联剂4g,升温至120℃,真空-0.1MPa条件下,脱水2小时,检测体系含水量少于0.05%为合格。
具体实施方式:
下面通过如下实例来对本发明进行进一步的详细说明:
实施例1:
A胶的制备:
(1)聚酯多元醇的制备:
在带有温度计、搅拌器、球式冷却器、氮气密封管的四口烧瓶中,加入间苯二甲酸120.6g,己二酸318.1g,葵二酸146.8g,环乙烷二甲醇704.7g,1.6- 己二醇352.4g和0.2~0.25g钛酸四丁酯催化剂,搅拌均匀,然后缓慢升温,在160℃~230℃下反应14小时后,取样测酸价,若酸价小于20mgKOH/g,则酯化合格,酯化合格后进行缩聚反应,在温度220~230℃条件下,在-0.1Mpa下抽真空5小时,得到酸价≤1mgKOH/g,羟值112±5mgKOH/g的聚酯多元醇。
(2)A胶的制备,将上述酯化缩聚后得到的聚酯多元醇100g,分子量1000 聚氧化丙烯二醇及100g,在120℃条件下真空脱水2小时,至体系含水量少于 0.05%,降温至40℃,加入4,4-二苯基甲烷二异氰酸酯(MDI)228.6g反应,, 温度控制在80℃±5℃,反应5小时,得粘度在6000mPa.s/25℃,NCO=14%的主胶。
B胶的制备:
取分子量400~2000的聚氧化丙烯四醇300g,蓖麻油500g和偶联剂4g,升温至120℃,真空-0.1MPa条件下,脱水2小时,检测体系含水量少于0.05%为合格。
将上述A胶与B胶按100:45配比,复合PET/AL/CPP,在50℃烘箱中熟化 48小时的强度为2.5N(外层)/5N(内层)。
Figure BDA0002872732210000031
而用市场上其他厂家复的膜剥离强度如下:
Figure BDA0002872732210000032
Figure BDA0002872732210000041
说明我公司产品加入高官能团聚醚和合成合适的聚酯多元醇,提高胶水的耐温性,同时解决了铝塑外层难题。
实施例2:
A胶的制备:
(1)聚酯多元醇的制备:
在带有温度计、搅拌器、球式冷却器、氮气密封管的四口烧瓶中,加入间苯二甲酸120.6g,己二酸318.1g,葵二酸146.8g,环乙烷二甲醇704.7g,1.6- 己二醇352.4g和0.2~0.25g钛酸四丁酯催化剂,搅拌均匀,然后缓慢升温,在160℃~230℃下反应14小时后,取样测酸价,若酸价小于20mgKOH/g,则酯化合格,酯化合格后进行缩聚反应,在温度220~230℃条件下,在-0.1Mpa下抽真空5小时,得到酸价≤1mgKOH/g,羟值112±5mgKOH/g的聚酯多元醇。
(2)A胶的制备,将上述酯化缩聚后得到的聚酯多元醇100g,分子量1000 聚氧化丙烯二醇及100g,在120℃条件下真空脱水2小时,至体系含水量少于 0.05%,降温至40℃,加入4,4-二苯基甲烷二异氰酸酯(MDI)251.6g反应,, 温度控制在80℃±5℃,反应5小时,得粘度在5000mPa.s/25℃,NCO=15%的主胶。
B胶的制备:
取分子量400~500的聚氧化丙烯五醇300g,蓖麻油500g和偶联剂4g,升温至120℃,真空-0.1MPa条件下,脱水2小时,检测体系含水量少于0.05%为合格。
将上述A胶与B胶按100:45配比,复合PET/AL/CPP,在50℃烘箱中熟化 48小时的强度为2.5N(外层)/5N(内层)。
Figure BDA0002872732210000042
Figure BDA0002872732210000051
而用市场上其他厂家复的膜剥离强度如下:
Figure BDA0002872732210000052
说明我公司产品加入高官能团聚醚和合成合适的聚酯多元醇,提高胶水的耐温性,同时解决了铝塑外层难题。
以上所述,仅为本发明较佳的具体实施方式,但本发明的保护范围并不局限于此,任何熟悉本技术领域的技术人员在本发明揭露的技术范围内,可轻易想到的变化或替换,都应涵盖在本发明的保护范围之内。因此,本发明的保护范围应该以权利要求书的保护范围为准。

Claims (2)

1.一种无溶剂双组份铝塑蒸煮胶粘剂,其特征在于:由A胶和B胶组成,A胶是由聚酯多元醇、液化MDI和聚醚多元醇反应而成,B胶是由含有高官能团聚醚多元醇、偶联剂和蓖麻油组成,A胶和B胶配比为100:45,
在所述无溶剂双组份铝塑蒸煮胶中,所述的聚酯多元醇是由含有小分子二元酸与二元醇缩聚而成;
在所述无溶剂双组份铝塑蒸煮胶中,所述的小分子二元酸为己二酸、间苯二甲酸、癸二酸、对苯二甲酸、邻苯二甲酸酐中的一种或两种的混合物。优选间苯二甲酸、己二酸或癸二酸,所述的二元醇为乙二醇、二乙二醇、新戊二醇、1,2丙二醇,甲基丙二醇、甘油、环己烷二甲醇、1,4-丁二醇、1,6-己二醇中的一种或两种的混合物。优选环己烷二甲醇和1,6-己二醇;
在所述无溶剂双组份铝塑蒸煮胶中,所述的聚醚多元醇为:平均分子量1000的聚氧化丙烯二醇,分子量400~2000的聚氧化丙烯四醇或分子量400~500的聚氧化丙烯五醇;
在所述无溶剂双组份铝塑蒸煮胶中,所述的硅烷偶联剂为:γ―氨丙基三乙氧基硅烷、γ―氨丙基三甲氧基硅烷、N-(2-氨乙基)-3-氨丙基三甲氧基硅烷、N-(2-氨乙基)-3-氨丙基三乙氧基硅烷、苯胺甲基三乙氧基硅烷、3-甲基丙烯酰氧丙基三甲氧基硅烷中的一种或两种以上的混合物。
2.根据权利要求1所述无溶剂双组份铝塑蒸煮胶的制备方法,其制备方法是:
(1)聚酯多元醇的制备:
在带有温度计、搅拌器、球式冷却器、氮气密封管的四口烧瓶中,加入间苯二甲酸120.6g,己二酸318.1g,葵二酸146.8g,环乙烷二甲醇704.7g,1.6-己二醇352.4g和0.2~0.25g钛酸四丁酯催化剂,搅拌均匀,然后缓慢升温,在160℃~230℃下反应14小时后,取样测酸价,若酸价小于20mgKOH/g,则酯化合格,酯化合格后进行缩聚反应,在温度220~230℃条件下,在-0.1Mpa下抽真空5小时,得到酸价≤1mgKOH/g,羟值112±5mgKOH/g的聚酯多元醇;
(2)A胶的制备,将上述酯化缩聚后得到的聚酯多元醇100g,分子量1000聚氧化丙烯二醇及100g,在120℃条件下真空脱水2小时,至体系含水量少于0.05%,降温至40℃,加入4,4-二苯基甲烷二异氰酸酯(MDI)228.6g与251.6g反应,,温度控制在80℃±5℃,反应5小时,得粘度在5000~6000mPa.s/25℃,NCO=14~15%的主胶;
B胶的制备:
取分子量400~2000的聚氧化丙烯四醇或分子量400~500的聚氧化丙烯五醇300g,蓖麻油500g和偶联剂4g,升温至120℃,真空-0.1MPa条件下,脱水2小时,检测体系含水量少于0.05%为合格。
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CN113619226A (zh) * 2021-07-30 2021-11-09 江阴市龙洋塑料包装有限公司 一种铝塑复合袋用黏性的铝膜材料及其生产工艺

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* Cited by examiner, † Cited by third party
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CN113619226A (zh) * 2021-07-30 2021-11-09 江阴市龙洋塑料包装有限公司 一种铝塑复合袋用黏性的铝膜材料及其生产工艺

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