CN104789098A - 一种环保高性能醇酸树脂 - Google Patents
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Abstract
本发明公开了一种环保高性能醇酸树脂，包括将地沟油、酸化油、三羟甲基丙烷、PAT水池料、涤纶废丝及甲基硅油投入反应釜中，升温至245-248℃进行点动搅拌，至没有阻力时开启搅拌并升温至275-282℃进行保温得到中间料，其中将料液中的水不断采用油水分离器分出,将偏硼酸锌与改性高岭土置于研磨机中高速分散研磨得到A物料，将中间料降温至240-245℃以下，加入固体石油树脂与A物料搅拌,抽往含芳烃的兑稀釜中进行搅拌，采用冷却水对兑稀釜冷却，用芳烃调整兑稀釜内粘度，过滤得到环保高性能醇酸树脂。本发明环保，成本低，硬度、光泽度及丰满度较优异，制备工艺简单，便于实际操作。
Description
技术领域
本发明涉及醇酸树脂技术领域，尤其涉及一种环保高性能醇酸树脂。
背景技术
醇酸树脂涂料可在常温下干燥，漆膜坚硬光亮，具有优良的耐候性，主要作为工业涂料和建筑涂料。在20世纪70年代以前，我国涂料的产品中醇酸树脂和醇酸调和漆最高占有70-80％的份额，近年来其市场份额减少至30％左右，石油等原材料价格持续上涨，在今天市场竞争日益激烈的涂料市场，生产性价比高的低成本树脂对涂料成本控制日趋迫切，且随着生活水平的提高，人们对生活质量的要求也日益严格，减轻环境压力，生产为生活环境减负的涂料产品也是势在必行。
发明内容
本发明提出了一种环保高性能醇酸树脂，上述环保高性能醇酸树脂环保，成本低，硬度、光泽度及丰满度较优异。
本发明提出的一种环保高性能醇酸树脂，包括：按重量份将13-17份地沟油、3-6份酸化油、以酸化油为基准45-65wt％三羟甲基丙烷、7-8.5份PAT水池料、13-17份涤纶废丝及以地沟油与酸化油总量为基准35-43wt％甲基硅油投入反应釜中，升温至245-248℃进行点动搅拌，至点动搅拌没有阻力时开启搅拌并以1-3℃/min升温速度升温至275-282℃进行保温得到中间料，上述过程中将料液中的水不断采用油水分离器分出，检测中间料的粘度为200-220s/25℃(涂-4)，检测中间料的酸价为≤10mgKOH/g；将2-4份偏硼酸锌与3-6份改性高岭土置于研磨机中高速分散研磨得到A物料，其中改性高岭土采用偶联剂KH-171进行改性，将中间料以4-6℃/min降温至240-245℃以下，加入A物料与甲基硅油为基准85-95wt％固体石油树脂与A物料搅拌2-5min，将得到的料液抽往含芳烃的兑稀釜中进行搅拌，芳烃与甲基硅油的重量比为25-30:5-8，搅拌过程中采用冷却水对兑稀釜冷却，冷却速度为10-14℃/min，待物料冷却至40-50℃时用芳烃调整兑稀釜内粘度为200-400s/25℃，过滤后得到环保高性能醇酸树脂。
优选地，按重量份将14-15份地沟油、3.5-4.2份酸化油、以酸化油为基准48-52wt％三羟甲基丙烷、7.5-8份PAT水池料、14-16份涤纶废丝及以地沟油与酸化油总量为基准38-39.5wt％甲基硅油投入反应釜中。
优选地，关闭人孔升温至246-247℃进行点动搅拌，至点动搅拌没有阻力时开启搅拌并以1.5-2℃/min升温速度升温至278-280℃进行保温得到中间料。
优选地，将中间料以4-6℃/min降温至243-244℃以下，开引风机，开人孔，加入A物料与甲基硅油为基准92-94wt％固体石油树脂搅拌2-3min。
优选地，芳烃与甲基硅油的重量比为26-28:6-8，搅拌过程中采用冷却水对兑稀釜冷却，冷却速度为13-14℃/min，待物料冷却至45-48℃时用芳烃调整兑稀釜内粘度为200-400s/25℃。
本发明中，上述环保高性能醇酸树脂有效解决了一些食品厂及日常生活产生的地沟油难处理、难回收问题，涤纶纺丝行业涤纶废丝脚料难回收、难处理问题，以及涤纶上游产品PTA在生产包装及运输过程中产生废料的难回收问题，变废为宝被充分利用，上述醇酸树脂既减少了工业浪费及缓解了一些工业废料难处理给环境造成的压力，又大幅度降低了涂料用成膜物质的成本，且制备工艺简单，大大降低了生产成本，且其干性良好，偏硼酸锌可阻挡水汽及其它腐蚀气体渗进涂膜或者具有化学抑制作用，改性高岭土可改善涂膜的耐磨、附着力、耐热性及增加涂膜厚度，增强涂膜的防腐效果，甲基硅油具有抗浮色、消泡作用，改善流挂的功能，偏硼酸锌、改性高岭土及甲基硅油配合作用，制品性能极为优异，成本低，且比传统389树脂具有更高的硬度、光泽度及丰满度，用于生产一些室内防腐涂料具有很高的性价比。
具体实施方式
实施例1
一种环保高性能醇酸树脂，包括：按重量份将13份地沟油、6份酸化油、以酸化油为基准45wt％三羟甲基丙烷、8.5份PAT水池料、13份涤纶废丝及以地沟油与酸化油总量为基准43wt％甲基硅油投入反应釜中，关闭人孔升温至245℃进行点动搅拌，至点动搅拌没有阻力时开启搅拌并以3℃/min升温速度升温至275℃进行保温得到中间料，上述过程中将料液中的水不断采用油水分离器分出，检测中间料的粘度为220s/25℃(涂-4)，检测中间料的酸价为≤10mgKOH/g；
将2份偏硼酸锌与6份改性高岭土置于研磨机中高速分散研磨得到A物料，其中改性高岭土采用偶联剂KH-171进行改性，将中间料以4℃/min降温至245℃以下，开引风机，开人孔，加入A物料与甲基硅油为基准85wt％固体石油树脂与A物料搅拌5min，将得到的料液抽往含芳烃的兑稀釜中进行搅拌，芳烃与甲基硅油的重量比为25:8，搅拌过程中采用冷却水对兑稀釜冷却，冷却速度为10℃/min，待物料冷却至50℃时用芳烃调整兑稀釜内粘度为250s/25℃，过滤后得到环保高性能醇酸树脂。
实施例2
一种环保高性能醇酸树脂，包括：按重量份将17份地沟油、3份酸化油、以酸化油为基准65wt％三羟甲基丙烷、7份PAT水池料、17份涤纶废丝及以地沟油与酸化油总量为基准35wt％甲基硅油投入反应釜中，关闭人孔升温至248℃进行点动搅拌，至点动搅拌没有阻力时开启搅拌并以1℃/min升温速度升温至282℃进行保温得到中间料，上述过程中将料液中的水不断采用油水分离器分出，检测中间料的粘度为200s/25℃(涂-4)，检测中间料的酸价为≤10mgKOH/g；
将4份偏硼酸锌与3份改性高岭土置于研磨机中高速分散研磨得到A物料，其中改性高岭土采用偶联剂KH-171进行改性，将中间料以6℃/min降温至240℃以下，开引风机，开人孔，加入A物料与甲基硅油为基准95wt％固体石油树脂与A物料搅拌2min，将得到的料液抽往含芳烃的兑稀釜中进行搅拌，芳烃与甲基硅油的重量比为30:5，搅拌过程中采用冷却水对兑稀釜冷却，冷却速度为14℃/min，待物料冷却至40℃时用芳烃调整兑稀釜内粘度为400s/25℃，过滤后得到环保高性能醇酸树脂。
实施例3
一种环保高性能醇酸树脂，包括：按重量份将14.3份地沟油、3.8份酸化油、以酸化油为基准51.5wt％三羟甲基丙烷、7.8份PAT水池料、15.8份涤纶废丝及以地沟油与酸化油总量为基准39wt％甲基硅油投入反应釜中，关闭人孔升温至246℃进行点动搅拌，至点动搅拌没有阻力时开启搅拌并以2℃/min升温速度升温至278℃进行保温得到中间料，上述过程中将料液中的水不断采用油水分离器分出，检测中间料的粘度为210s/25℃(涂-4)，检测中间料的酸价为≤10mgKOH/g；
将2.5份偏硼酸锌与5份改性高岭土置于研磨机中高速分散研磨得到A物料，其中改性高岭土采用偶联剂KH-171进行改性，将中间料以5℃/min降温至243℃以下，开引风机，开人孔，加入A物料与甲基硅油为基准93.5wt％固体石油树脂搅拌2.5min，将得到的料液抽往含芳烃的兑稀釜中进行搅拌，芳烃与甲基硅油的重量比为27:7，搅拌过程中采用冷却水对兑稀釜冷却，冷却速度为13.5℃/min，待物料冷却至47℃时用芳烃调整兑稀釜内粘度为350s/25℃，过滤后得到环保高性能醇酸树脂。
实施例4
一种环保高性能醇酸树脂，包括：按重量份将16份地沟油、4份酸化油、以酸化油为基准62wt％三羟甲基丙烷、7.8份PAT水池料、16.5份涤纶废丝及以地沟油与酸化油总量为基准42wt％甲基硅油投入反应釜中，关闭人孔升温至247℃进行点动搅拌，至点动搅拌没有阻力时开启搅拌并以1.5℃/min升温速度升温至278℃进行保温得到中间料，上述过程中将料液中的水不断采用油水分离器分出，检测中间料的粘度为215s/25℃(涂-4)，检测中间料的酸价为≤10mgKOH/g；
将2.5份偏硼酸锌与5.5份改性高岭土置于研磨机中高速分散研磨得到A物料，其中改性高岭土采用偶联剂KH-171进行改性，将中间料以5℃/min降温至242℃以下，开引风机，开人孔，加入A物料与甲基硅油为基准92wt％固体石油树脂与A物料搅拌4min，将得到的料液抽往含芳烃的兑稀釜中进行搅拌，芳烃与甲基硅油的重量比为28:8，搅拌过程中采用冷却水对兑稀釜冷却，冷却速度为11℃/min，待物料冷却至48℃时用芳烃调整兑稀釜内粘度为300s/25℃，过滤后得到环保高性能醇酸树脂。
测定实施例1-4中所述中间料酸价与粘度时，首先将60g芳烃溶剂加75g中间料中混合均匀，测试得到的物料的酸价与25℃时的粘度即为中间料的酸价与粘度。
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，根据本发明的技术方案及其发明构思加以等同替换或改变，都应涵盖在本发明的保护范围之内。
Claims (5)
1.一种环保高性能醇酸树脂，其特征在于，按重量份将13-17份地沟油、3-6份酸化油、以酸化油为基准45-65wt％三羟甲基丙烷、7-8.5份PAT水池料、13-17份涤纶废丝、以地沟油与酸化油总量为基准35-43wt％甲基硅油投入反应釜中，升温至245-248℃进行点动搅拌，至点动搅拌没有阻力时开启搅拌并以1-3℃/min升温速度升温至275-282℃进行保温得到中间料，上述过程中将料液中的水不断采用油水分离器分出，检测中间料的粘度为200-220s/25℃(涂-4)，检测中间料的酸价为≤10mgKOH/g；将2-4份偏硼酸锌与3-6份改性高岭土置于研磨机中高速分散研磨得到A物料，其中改性高岭土采用偶联剂KH-171进行改性，将中间料以4-6℃/min降温至240-245℃以下，加入A物料与甲基硅油为基准85-95wt％固体石油树脂与A物料搅拌2-5min，将得到的料液抽往含芳烃的兑稀釜中进行搅拌，芳烃与甲基硅油的重量比为25-30:5-8，搅拌过程中采用冷却水对兑稀釜冷却，冷却速度为10-14℃/min，待物料冷却至40-50℃时用芳烃调整兑稀釜内粘度为200-400s/25℃，过滤后得到环保高性能醇酸树脂。
2.根据权利要求1所述的环保高性能醇酸树脂，其特征在于，按重量份将14-15份地沟油、3.5-4.2份酸化油、以酸化油为基准48-52wt％三羟甲基丙烷、7.5-8份PAT水池料、14-16份涤纶废丝及以地沟油与酸化油总量为基准38-39.5wt％甲基硅油投入反应釜中。
3.根据权利要求1所述的环保高性能醇酸树脂，其特征在于，升温至246-247℃进行点动搅拌，至点动搅拌没有阻力时开启搅拌并以1.5-2℃/min升温速度升温至278-280℃进行保温得到中间料。
4.根据权利要求1所述的环保高性能醇酸树脂，其特征在于，将中间料以4-6℃/min降温至243-244℃以下，开引风机，开人孔，加入A物料与甲基硅油为基准92-94wt％固体石油树脂搅拌2-3min。
5.根据权利要求1所述的环保高性能醇酸树脂，其特征在于，芳烃与甲基硅油的重量比为26-28:6-8，搅拌过程中采用冷却水对兑稀釜冷却，冷却速度为13-14℃/min，待物料冷却至45-48℃时用芳烃调整兑稀釜内粘度为200-400s/25℃。
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