CN104448206A - 一种环保型可剥离水性聚氨酯树脂及其制备方法和应用 - Google Patents
一种环保型可剥离水性聚氨酯树脂及其制备方法和应用 Download PDFInfo
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Abstract
本发明属于水性聚氨酯制备技术领域,公开了一种环保型可剥离水性聚氨酯树脂及其制备方法和应用。该制备方法包括以下具体步骤:将脱水后的低聚物二元醇与二异氰酸酯混合加热反应;加入小分子扩链剂、亲水扩链剂,加热反应;搅拌下依次加入中和剂、潜固化剂、水、后扩链剂,搅拌均匀,即得到环保型可剥离水性聚氨酯树脂;所述的潜固化剂包括封闭型异氰酸酯类和含环氧基的硅氧烷中的至少一种。本发明体系中加入了潜固化剂,在乳液成膜的过程中与树脂体系中存在的亲水性基团反应从而去除亲水基团,赋予树脂极佳的耐水性,且潜固化剂在成膜过程中再次交联固化,进一步提高树脂的综合性能,延长涂膜的使用寿命,提供长期有效的保护性能。
Description
技术领域
本发明属于水性聚氨酯制备技术领域,特别涉及一种环保型可剥离水性聚氨酯树脂及其制备方法和应用。
背景技术
随着生活水平的不断提高,人们对产品的外观、环保性及其使用性能等要求也在日益增加。制造商会在玻璃、陶瓷、金属建材等材料表面附加一层保护涂料,以避免其在加工、运输以及组装等过程中被刮伤,以至影响其美观度,甚至降低其性能。
目前市场上大部分可剥离涂料使用的基础树脂仍是溶剂型的,其在生产、施工及使用过程中均会对环境及人体造成污染和伤害,有悖于绿色环保的发展理念。虽有小部分水性产品在使用,但是也暴露出不少的问题:(1)在使用过程中,涂层与基材不能始终粘合在一起,易脱落;(2)涂层强度不够,不易整片剥离;(3)亲水扩链剂作为内乳化剂,对乳液的稳定性起着至关重要的作用,但是涂膜干燥后,其极易吸水,使得涂层耐水性较差,吸水后易泛白,大大降低了涂膜对基材的保护效果;(4)涂层耐酸碱以及耐高低温性能差等。
发明内容
为了克服上述现有技术的缺点与不足,本发明的首要目的在于提供一种环保型可剥离水性聚氨酯树脂的制备方法。
本发明另一目的在于提供上述方法制备的环保型可剥离水性聚氨酯树脂。
本发明再一目的在于提供上述环保型可剥离水性聚氨酯树脂在表面防护领域中的应用,特别适用于玻璃、陶瓷及金属建材表面保护中。
本发明的目的通过下述方案实现:
一种环保型可剥离水性聚氨酯树脂的制备方法,包括以下具体步骤:
(1)将脱水后的低聚物二元醇与二异氰酸酯混合加热反应;
(2)加入小分子扩链剂、亲水扩链剂,加热反应;
(3)搅拌下依次加入中和剂、潜固化剂、水、后扩链剂,搅拌均匀,即得到环保型可剥离水性聚氨酯树脂。
所述的潜固化剂包括封闭型异氰酸酯类和含环氧基的硅氧烷中的至少一种。优选地,所用潜固化剂与低聚物二元醇的质量比为(0.5~1.5):(20~60)。
为了更好地实现本发明,所述的含环氧基的硅氧烷不含氨基、羟基或者硫醇基等带有活泼氢的基团。
本发明所述的低聚物多元醇优选为分子量为400~4000的聚酯型或者聚醚型二元醇,可包括聚己二酸丁二醇酯二醇、聚己内酯二醇、聚碳酸酯二醇、聚四氢呋喃醚二醇和聚丙二醇等中的至少一种,其中包括至少一种的聚醚多元醇。
优选地,本发明所述的二异氰酸酯并无特别限制,已知使用的二异氰酸酯均可,可为异佛尔酮二异氰酸酯(IPDI)、六次甲基二异氰酸酯(HDI)、甲苯二异氰酸酯(TDI)和4,4-二环己基甲烷二异氰酸酯(H12-MDI)等中的至少一种。
优选地,本发明所述的小分子扩链剂并无特别限制,已知使用的小分子扩链剂均可,为了更好地实现本发明,所述的小分子扩链剂优选为1,4-丁二醇(BDO)、新戊二醇(NPG)、1,6-己二醇(HEG)和一缩二乙二醇中的至少一种,其用量为催化量即可。
优选地,本发明所述的亲水扩链剂并无特别限制,已知使用的亲水扩链剂均可,为了更好地实现本发明,所述的亲水扩链剂优选为二羟甲基丙酸、二羟甲基丁酸和双羟基磺酸盐中的至少一种,其用量为催化量即可。
本发明所述的中和剂用于调节反应体系的pH值至弱碱性,可为本领域任意常用的碱液,如三甲胺、三乙胺、氨水等。
本发明所述的后扩链剂并无特别限制,已知使用的后扩链剂均可,为了更好地实现本发明,所述的后扩链剂优选为乙二胺、丙二胺、1,6-己二胺、二亚乙基三胺、异氟尔酮二胺和三亚乙基四胺中的至少一种。
为了进一步更好地实现本发明,上述制备方法过程中各组分的用量优选为:
上述制备方法优选在惰性气体保护下进行。
步骤(1)中所述的加热反应优选在60~90℃下,搅拌反应1.5~2.5 h。
步骤(1)中所述的脱水优选在80~140℃下脱水2 h。
步骤(2)中的试剂添加前优选降低反应体系的温度至40~60℃。
步骤(2)中所述的加热反应优选加热至70~85℃,反应2.5~4.5 h。
步骤(3)中的试剂添加前优选降低反应体系的温度至50℃以下。
步骤(3)中所述依次加入中和剂、潜固化剂、水、后扩链剂,优选每次加入一种试剂后进行充分搅拌再加入下一种试剂,优选加入中和剂、潜固化剂后分别搅拌1~5 min,加入水、后扩链剂后分别高速搅拌10~30 min,加入水后进行高速搅拌可使体系充分乳化。
步骤(3)中添加水主要用于调节体系的固含,可根据实际生产需要进行任意的条件,因此其用量可根据需要调整,适量即可,优选使用120~280重量份。
优选地,上述所用小分子扩链剂和亲水扩链剂的总量为2.5~7.5重量份。
上述制备方法得到的环保型可剥离水性聚氨酯树脂,具有环保易剥离、稳定性好、持久可剥、强度高、耐水性极佳、良好的耐酸碱性以及耐高低温性能、产品成本低等优点,为环保型可剥涂料提供了高性价比的基础树脂,可广泛的用于表面防护领域中,特别适用于玻璃、陶瓷及金属建材表面保护中。
本发明的机理为:
本发明的环保型可剥离水性聚氨酯树脂选材独具匠心,体系中加入了潜固化剂,在乳液成膜的过程中与树脂体系中存在的亲水性基团反应从而去除制备过程中引入的亲水基团,从而赋予树脂极佳的耐水性,并消除了现有水性聚氨酯体系中存在的大量游离亲水基团而导致树脂极易吸水,使得涂层耐水性较差,吸水后易泛白,大大降低了涂膜对基材的保护效果的影响,并且由于这些酸性亲水基团的存在,导致涂膜的耐水解性能下降,降低涂膜的使用寿命,使其不能提供长期有效的保护功能;且本发明的潜固化剂在成膜过程中会再次交联固化,从而进一步提高了环保型可剥离水性聚氨酯树脂的综合性能。同时,本发明优选使用聚醚多元醇和聚酯多元醇进行混合制备树脂,从而获得优异的各项性能。
本发明相对于现有技术,具有如下的优点及有益效果:
(1)本发明的环保型可剥离水性聚氨酯树脂中加入了潜固化剂,在乳液成膜过程中既消除体系中的亲水基团,又相互交联固化,从而提高树脂的各项性能。
(2)本发明的环保型可剥离水性聚氨酯树脂合成工艺简单,可控性强,对设备的要求明显降低,同时避免了多重改性产品在合成过程中所带来的诸多影响因素。
(3)本发明的环保型可剥离水性聚氨酯树脂分散介质为水,成本较低,为水性环保可剥离涂料的制备提供了高性价比的基础树脂。
具体实施方式
下面结合实施例对本发明作进一步详细的描述,但本发明的实施方式不限于此。
实施例1:环保型可剥离水性聚氨酯树脂的制备
在干燥氮气保护下,将120℃下真空脱水2 h后的聚四氢呋喃醚二醇80克,异佛尔酮二异氰酸酯26.7克,加入反应器中,在机械搅拌下控制温度在70~90℃进行反应2小时;加入一缩二乙二醇5.6克,二羟甲基丙酸3.5克,在70~85℃反应3小时;降至50℃以下,加入计量三乙胺2.45克调节体系pH为弱碱性,继续搅拌5分钟;加入封闭型异氰酸酯类潜固化剂(TPA-B80X)0.7克,继续搅拌5分钟;加入水200克,高速(转速优选≥1200 r/min)分散10分钟;加入乙二胺1.5克,继续高速分散30分钟,即可得到环保型可剥离水性聚氨酯树脂。
实施例2:环保型可剥离水性聚氨酯树脂的制备
在干燥氮气保护下,将120℃下真空脱水2 h后的聚四氢呋喃醚二醇40克,聚丙二醇40克,异佛尔酮二异氰酸酯44.4克,加入反应器中,在机械搅拌下控制温度在70~90℃进行反应2小时;加入一缩二乙二醇4.0克,二羟甲基丙酸5.0克,在70~85℃反应3小时;降至50℃以下,加入计量三乙胺2.45克,继续搅拌5分钟;加入封闭型异氰酸酯类潜固化剂(TPA-B80X)4.5克,继续搅拌5分钟;加入水200克,高速分散10分钟;加入乙二胺1.5克,继续高速分散30分钟,即可得到环保型可剥离水性聚氨酯树脂。
实施例3:环保型可剥离水性聚氨酯树脂的制备
在干燥氮气保护下,将120℃下真空脱水2 h后的聚己内酯二醇40克,聚己二酸丁二醇酯二醇40克,甲苯二异氰酸酯34.8克,加入反应器中,在机械搅拌下控制温度在70~90℃进行反应2小时;加入一缩二乙二醇5.6克,二羟甲基丙酸3.5克,在70~85℃反应3小时;降至50℃以下,加入计量三乙胺2.45克,继续搅拌5分钟;加入环氧基硅氧烷类潜固化剂(OS-9012)2.8克,继续搅拌5分钟;加入水200克,高速分散10分钟;加入乙二胺1.5克,继续高速分散30分钟,即可得到环保型可剥离水性聚氨酯树脂。
实施例4:环保型可剥离水性聚氨酯树脂的制备
在干燥氮气保护下,将120℃下真空脱水2 h后的聚碳酸酯二元醇40克,聚四氢呋喃醚二醇40克,异佛尔酮二异氰酸酯22.2克,六次甲基二异氰酸酯16.8克,加入反应器中,在机械搅拌下控制温度在70~90℃进行反应2小时;加入1,4-丁二醇4.75克,二羟甲基丙酸3.5克,在70~85℃反应3小时;降至50℃以下,加入计量三乙胺2.45克,继续搅拌5分钟;加入封闭型异氰酸酯类潜固化剂(TPA-B80X)6.0克,继续搅拌5分钟;加入水200克,高速分散10分钟;加入乙二胺1.5克,继续高速分散30分钟,即可得到环保型可剥离水性聚氨酯树脂。
实施例5:环保型可剥离水性聚氨酯树脂的制备
在干燥氮气保护下,将120℃下真空脱水2 h后的聚碳酸酯二元醇40克,聚四氢呋喃醚二醇40克,4,4-二环己基甲烷二异氰酸酯104.8克,六次甲基二异氰酸酯16.8克,加入反应器中,在机械搅拌下控制温度在70~90℃进行反应2小时;加入1,4-丁二醇17.5克,二羟甲基丙酸10.0克,在70~85℃反应3小时;降至50℃以下,加入计量三乙胺2.45克,继续搅拌5分钟;加入环氧基硅氧烷(OS-9012)1.8克,继续搅拌5分钟;加入水200克,高速分散10分钟;加入乙二胺1.5克,继续高速分散30分钟,即可得到环保型可剥离水性聚氨酯树脂。
上述实施例为本发明较佳的实施方式,但本发明的实施方式并不受上述实施例的限制,其他的任何未背离本发明的精神实质与原理下所作的改变、修饰、替代、组合、简化,均应为等效的置换方式,都包含在本发明的保护范围之内。
Claims (10)
1.一种环保型可剥离水性聚氨酯树脂的制备方法,其特征在于包括以下具体步骤:
(1)将脱水后的低聚物二元醇与二异氰酸酯混合加热反应;
(2)加入小分子扩链剂、亲水扩链剂,加热反应;
(3)搅拌下依次加入中和剂、潜固化剂、水、后扩链剂,搅拌均匀,即得到环保型可剥离水性聚氨酯树脂;
所述的潜固化剂包括封闭型异氰酸酯类和含环氧基的硅氧烷中的至少一种。
2.根据权利要求1所述的环保型可剥离水性聚氨酯树脂的制备方法,其特征在于:所述的含环氧基的硅氧烷不含氨基、羟基或者硫醇基的带有活泼氢的基团。
3.根据权利要求1所述的环保型可剥离水性聚氨酯树脂的制备方法,其特征在于:所用潜固化剂与低聚物二元醇的质量比为(0.5~1.5):(20~60)。
4.根据权利要求1所述的环保型可剥离水性聚氨酯树脂的制备方法,其特征在于:所述的低聚物多元醇包括分子量为400~4000的聚酯型或者聚醚型二元醇。
5.根据权利要求1所述的环保型可剥离水性聚氨酯树脂的制备方法,其特征在于:所述的低聚物多元醇包括聚己二酸丁二醇酯二醇、聚己内酯二醇、聚碳酸酯二醇、聚四氢呋喃醚二醇和聚丙二醇中的至少一种,其中包括至少一种的聚醚多元醇。
6.根据权利要求1所述的环保型可剥离水性聚氨酯树脂的制备方法,其特征在于:所述的二异氰酸酯包括异佛尔酮二异氰酸酯、六次甲基二异氰酸酯、甲苯二异氰酸酯和4,4-二环己基甲烷二异氰酸酯中的至少一种;所述的小分子扩链剂包括1,4-丁二醇、新戊二醇、1,6-己二醇和一缩二乙二醇中的至少一种;所述的亲水扩链剂包括二羟甲基丙酸、二羟甲基丁酸和双羟基磺酸盐中的至少一种;所述的后扩链剂包括乙二胺、丙二胺、1,6-己二胺、二亚乙基三胺、异氟尔酮二胺和三亚乙基四胺中的至少一种。
7.根据权利要求1所述的环保型可剥离水性聚氨酯树脂的制备方法,其特征在于所述制备方法过程中各组分的用量为:
8.根据权利要求1所述的环保型可剥离水性聚氨酯树脂的制备方法,其特征在于:步骤(1)中所述的加热反应指在60~90℃下,搅拌反应1.5~2.5h;步骤(2)中所述的加热反应为加热至70~85℃,反应2.5~4.5h。
9.一种环保型可剥离水性聚氨酯树脂,其特征在于根据权利要求1~8任一项所述的环保型可剥离水性聚氨酯树脂的制备方法得到。
10.根据权利要求9所述的环保型可剥离水性聚氨酯树脂在表面防护领域中的应用。
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