CN106479603A - 一种粘度指数改进剂组合物及其制备方法 - Google Patents

一种粘度指数改进剂组合物及其制备方法 Download PDF

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CN106479603A
CN106479603A CN201610831315.XA CN201610831315A CN106479603A CN 106479603 A CN106479603 A CN 106479603A CN 201610831315 A CN201610831315 A CN 201610831315A CN 106479603 A CN106479603 A CN 106479603A
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styrene
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王稳
张柄
豆素琴
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Xijing University
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Abstract

一种粘度指数改进剂组合物及其制备方法,将基础油加入调合釜加温至80℃;然后将占总质量(8~45)%的乙丙共聚物和占总质量的(45~80)%的氢化苯乙烯双烯共聚物分别切成胶粒,粒度为3cm;最后将得到胶粒加入到升温后的基础油中,继续加热到120℃,同时搅拌至胶粒全部溶解,搅拌时间至少12小时,完全溶解后降温至80℃出釜灌装,得到粘度指数改进剂组合物;本发明具有高温粘度永久性下降慢,低温条件下不发生聚凝的特点。

Description

一种粘度指数改进剂组合物及其制备方法
技术领域
本发明属于润滑油技术领域,具体涉及一种粘度指数改进剂组合物及其制备方法。
背景技术
为了满足内燃机油油品的高、低温性能,需要在所使用的较低粘度的基础油中加入油溶性链状高分子聚合物,即粘度指数改进剂,也叫增粘剂,粘度指数改进剂不仅能稠化基础油,改善油品的粘温性能,使油品具有良好的高温润滑性和低温流动性。
常用的粘度指数改进剂有聚甲基丙烯酸酯(PMA)、聚异丁烯(PIB)、乙丙共聚物(OCP)、氢化苯乙烯双烯共聚物(HSD)、苯乙烯聚酯和聚正丁基乙烯基醚(BB)等。OCP型粘度指数改进剂具有增粘能力和剪切稳定性较好、高温性能好及现场使用性能好等特点,价格也适中,是目前世界上用得较多的一个品种。
但是OCP型粘度指数改进剂高温抗降解能力差,在发动机油中使用时,受到长时间高温影响,粘度永久性下降过快,大大降低发动机油的使用性能,严重者造成发动机机油压力下降,发动机磨损;同时OCP型粘度指数改进剂在低温条件下发生聚凝,并且不能采用降凝剂改变聚凝问题,大大影响低温性能。
HSD是嵌段或星状聚合物,有优良的稠化能力和剪切稳定性,低温下不发生聚凝,但由于其苯乙烯部分易热解,在柴油机油中使用性能不好,加上价格较贵,因此影响了其广泛使用。
所以单一的、常规的粘度指数改进剂并不能适应热负荷较高的发动机的运行要求,需要一种在高温条件下能够保持稳定粘度的粘度指数改进剂、高温粘度变化率小、低温条件下不发生聚凝的粘度指数改进剂方案。
发明内容
为了克服上述现有技术的缺点,本发明的目的在于提供一种粘度指数改进剂组合物及其制备方法,高温粘度永久性下降慢,低温条件下不发生聚凝,具有极好的高温剪切性能,同时能保证油品氧化安定性和清净性优异。
为了达到上述目的,本发明采取的技术方案是:
一种粘度指数改进剂组合物,原料组成为乙丙共聚物占总质量的(8~45)%,氢化苯乙烯双烯共聚物占总质量的(45~80)%,其余为基础油。
所述的乙丙共聚物是乙烯和丙烯的二元共聚物,由乙烯和丙烯聚合而成,其中乙烯质量含量48%~53%。
所述的氢化苯乙烯双烯共聚物是一种固体星型苯乙烯共聚物,苯乙烯和异戊二烯的星型共聚物,其中苯乙烯质量含量55%~65%,分子量在5~11万。
所述的基础油为加氢精制基础油。
一种粘度指数改进剂组合物的制备方法,包括以下步骤:
步骤一:将基础油加入调合釜加温至80℃;
步骤二:将占总质量(8~45)%的乙丙共聚物和占总质量的(45~80)%的氢化苯乙烯双烯共聚物分别切成胶粒,粒度为3cm;
步骤三:将步骤二得到的胶粒加入到步骤一中升温后的基础油中,继续加热到120℃,同时搅拌至胶粒全部溶解,搅拌时间至少12小时,完全溶解后降温至80℃出釜灌装,得到粘度指数改进剂组合物;
所述的乙丙共聚物是乙烯和丙烯的二元共聚物,由乙烯和丙烯聚合而成,其中乙烯质量含量48%~53%;
所述的氢化苯乙烯双烯共聚物是一种固体星型苯乙烯共聚物,苯乙烯和异戊二烯的星型共聚物,其中苯乙烯质量含量55%~65%,分子量在5~11万;
所述的基础油为加氢精制基础油。
本发明的有益效果:乙丙共聚物与氢化苯乙烯双烯共聚物按比例配比,既能防止乙丙共聚物在发动机油中使用时,受到长时间高温影响,粘度永久性下降过快,造成发动机机油压力下降,发动机磨损,又能克服低温聚凝的现象。
具体实施方式
本发明的技术效果通过下面实施例进一步说明。
实施例1
一种粘度指数改进剂组合物,原料组成为乙丙共聚物占总质量的8.75%,氢化苯乙烯双烯共聚物占总质量的78.75%,基础油占总质量的12.50%;
所述的乙丙共聚物是乙烯和丙烯的二元共聚物,由乙烯和丙烯在一定工艺下聚合而成,其中乙烯质量含量48%;所述的氢化苯乙烯双烯共聚物是一种固体星型苯乙烯共聚物,苯乙烯和异戊二烯的星型共聚物,其中苯乙烯质量含量55%;
所述的基础油为加氢精制基础油。
一种粘度指数改进剂组合物的制备方法,包括以下步骤:
步骤一:将占总质量12.50%的基础油加入调合釜加温至80℃;
步骤二:将占总质量8.75%的乙丙共聚物和占总质量78.75%的氢化苯乙烯双烯共聚物分别切成胶粒,粒度为3cm;
步骤三:将步骤二得到的胶粒加入到步骤一中升温后的基础油中,继续加热到120℃,同时搅拌至胶粒全部溶解,搅拌时间至少12小时,完全溶解后降温至80℃出釜灌装,得到粘度指数改进剂组合物;
所述的乙丙共聚物是乙烯和丙烯的二元共聚物,由乙烯和丙烯在一定工艺下聚合而成,其中乙烯质量含量48%;所述的氢化苯乙烯双烯共聚物是一种固体星型苯乙烯共聚物,苯乙烯和异戊二烯的星型共聚物,其中苯乙烯含量55%;
所述的基础油为加氢精制基础油。
实施例2
一种粘度指数改进剂组合物,原料组成为乙丙共聚物占总质量的17.5%,氢化苯乙烯双烯共聚物占总质量的70.0%,基础油占总质量的12.5%;
所述的乙丙共聚物是乙烯和丙烯的二元共聚物,由乙烯和丙烯在一定工艺下聚合而成,其中乙烯质量含量49%;所述的氢化苯乙烯双烯共聚物是一种固体星型苯乙烯共聚物,苯乙烯和异戊二烯的星型共聚物,其中苯乙烯质量含量57%;
所述的基础油为加氢精制基础油。
一种粘度指数改进剂组合物的制备方法,包括以下步骤:
步骤一:将占总质量的12.5%基础油加入调合釜加温至80℃;
步骤二:将占总质量17.5%的乙丙共聚物和占总质量的70.0%氢化苯乙烯双烯共聚物分别切成胶粒,粒度为3cm;
步骤三:将步骤二得到的胶粒加入到步骤一中升温后的基础油中,继续加热到120℃,同时搅拌至胶粒全部溶解,搅拌时间至少12小时,完全溶解后降温至80℃出釜灌装,得到粘度指数改进剂组合物;
所述的乙丙共聚物是乙烯和丙烯的二元共聚物,由乙烯和丙烯在一定工艺下聚合而成,其中乙烯质量含量49%;所述的氢化苯乙烯双烯共聚物是一种固体星型苯乙烯共聚物,苯乙烯和异戊二烯的星型共聚物,其中苯乙烯质量含量57%;
所述的基础油为加氢精制基础油。
实施例3
一种粘度指数改进剂组合物,原料组成为乙丙共聚物占总质量的26.25%,氢化苯乙烯双烯共聚物占总质量的61.25%,基础油占总质量的12.50%;
所述的乙丙共聚物是乙烯和丙烯的二元共聚物,由乙烯和丙烯在一定工艺下聚合而成,其中乙烯质量含量50%;所述的氢化苯乙烯双烯共聚物是一种固体星型苯乙烯共聚物,苯乙烯和异戊二烯的星型共聚物,其中苯乙烯质量含量59%;
所述的基础油为加氢精制基础油。
一种粘度指数改进剂组合物的制备方法,包括以下步骤:
步骤一:将占总质量的12.5%基础油加入调合釜加温至80℃;
步骤二:将占总质量17.5%的乙丙共聚物和占总质量的70%氢化苯乙烯双烯共聚物分别切成胶粒,粒度为3cm;
步骤三:将步骤二得到的胶粒加入到步骤一中升温后的基础油中,继续加热到120℃,同时搅拌至胶粒全部溶解,搅拌时间至少12小时,完全溶解后降温至80℃出釜灌装,得到粘度指数改进剂组合物;
所述的乙丙共聚物是乙烯和丙烯的二元共聚物,由乙烯和丙烯在一定工艺下聚合而成,其中乙烯质量含量50%;所述的氢化苯乙烯双烯共聚物是一种固体星型苯乙烯共聚物,苯乙烯和异戊二烯的星型共聚物,其中苯乙烯质量含量59%;
所述的基础油为加氢精制基础油。
实施例4
一种粘度指数改进剂组合物,原料组成为乙丙共聚物占总质量的35%,氢化苯乙烯双烯共聚物占总质量的52.5%,基础油占总质量的12.5%;
所述的乙丙共聚物是乙烯和丙烯的二元共聚物,由乙烯和丙烯在一定工艺下聚合而成,其中乙烯质量含量52%;所述的氢化苯乙烯双烯共聚物是一种固体星型苯乙烯共聚物,苯乙烯和异戊二烯的星型共聚物,其中苯乙烯质量含量62%;
所述的基础油为加氢精制基础油。
一种粘度指数改进剂组合物的制备方法,包括以下步骤:
步骤一:将占总质量的12.5%基础油加入调合釜加温至80℃;
步骤二:将占总质量35%的乙丙共聚物和占总质量的52.5%氢化苯乙烯双烯共聚物分别切成胶粒,粒度为3cm;
步骤三:将步骤二得到的胶粒加入到步骤一中升温后的基础油中,继续加热到120℃,同时搅拌至胶粒全部溶解,搅拌时间至少12小时,完全溶解后降温至80℃出釜灌装,得到粘度指数改进剂组合物;
所述的乙丙共聚物是乙烯和丙烯的二元共聚物,由乙烯和丙烯在一定工艺下聚合而成,其中乙烯质量含量52%;所述的氢化苯乙烯双烯共聚物是一种固体星型苯乙烯共聚物,苯乙烯和异戊二烯的星型共聚物,其中苯乙烯质量含量62%;
所述的基础油为加氢精制基础油。
实施例5
一种粘度指数改进剂组合物,原料组成为乙丙共聚物占总质量的43.75%,氢化苯乙烯双烯共聚物占总质量的43.75%,基础油占总质量的12.50%;
所述的乙丙共聚物是乙烯和丙烯的二元共聚物,由乙烯和丙烯在一定工艺下聚合而成,其中乙烯质量含量53%;所述的氢化苯乙烯双烯共聚物是一种固体星型苯乙烯共聚物,苯乙烯和异戊二烯的星型共聚物,其中苯乙烯质量含量65%;
所述的基础油为加氢精制基础油。
一种粘度指数改进剂组合物的制备方法,包括以下步骤:
步骤一:将占总质量的12.50%基础油加入调合釜加温至80℃;
步骤二:将占总质量43.75%的乙丙共聚物和占总质量的43.75%氢化苯乙烯双烯共聚物分别切成胶粒,粒度为3cm;
步骤三:将步骤二得到的胶粒加入到步骤一中升温后的基础油中,继续加热到120℃,同时搅拌至胶粒全部溶解,搅拌时间至少12小时,完全溶解后降温至80℃出釜灌装,得到粘度指数改进剂组合物;
所述的乙丙共聚物是乙烯和丙烯的二元共聚物,由乙烯和丙烯在一定工艺下聚合而成,其中乙烯质量含量53%;所述的氢化苯乙烯双烯共聚物是一种固体星型苯乙烯共聚物,苯乙烯和异戊二烯的星型共聚物,其中苯乙烯质量含量65%;
所述的基础油为加氢精制基础油。
对比例1
现有技术的粘度指数改进剂,取乙丙共聚物87.5%份基础油12.5%。
对比例2
现有技术的粘度指数改进剂,取氢化苯乙烯双烯共聚物87.5%,基础油12.5%。
表1.高温氧化试验结果
参照表1所示,实施例1-5试验结果表明:得到粘度指数改进剂组合物,具有较低的100℃运动粘度变化率,并且通过CCS试验结果可以看出具有更好的低温性能,并且较低含量也可以防止油品低温聚凝,可见乙丙共聚物和氢化苯乙烯双烯共聚物混合调和的粘度指数改进剂具有良好的增效作用,大大提高了OCP的低温性能和高温抗降解性能。从成本上来讲,性价比较单纯使用氢化苯乙烯双烯共聚物更加优异。

Claims (8)

1.一种粘度指数改进剂组合物,其特征在于,原料组成为乙丙共聚物占总质量的(8~45)%,氢化苯乙烯双烯共聚物占总质量的(45~80)%,其余为基础油。
2.根据权利要求1所述的一种粘度指数改进剂组合物,其特征在于,所述的乙丙共聚物是乙烯和丙烯的二元共聚物,其中乙烯质量含量48%~53%。
3.根据权利要求1所述的一种粘度指数改进剂组合物,其特征在于,所述的氢化苯乙烯双烯共聚物是一种固体星型苯乙烯共聚物,苯乙烯和异戊二烯的星型共聚物,其中苯乙烯质量含量55%~65%,分子量在5~11万。
4.根据权利要求1所述的一种粘度指数改进剂组合物,其特征在于,所述的基础油为加氢精制基础油。
5.一种粘度指数改进剂组合物的制备方法,其特征在于,包括以下步骤:
步骤一:将基础油加入调合釜加温至80℃;
步骤二:将占总质量(8~45)%的乙丙共聚物和占总质量的(45~80)%氢化苯乙烯双烯共聚物分别切成胶粒,粒度为3cm;
步骤三:将步骤二得到的胶粒加入到步骤一中升温后的基础油中,继续加热到120℃,同时搅拌至胶粒全部溶解,搅拌时间至少12小时,完全溶解后降温至80℃出釜灌装,得到粘度指数改进剂组合物。
6.根据权利要求5所述的一种粘度指数改进剂组合物的制备方法,其特征在于,所述的乙丙共聚物是乙烯和丙烯的二元共聚物,由乙烯和丙烯在一定工艺下聚合而成,其中乙烯质量含量48%~53%。
7.根据权利要求5所述的一种粘度指数改进剂组合物的制备方法,其特征在于,所述的氢化苯乙烯双烯共聚物是一种固体星型苯乙烯共聚物,苯乙烯和异戊二烯的星型共聚物,其中苯乙烯质量含量55%~65%,分子量在5~11万。
8.根据权利要求5所述的一种粘度指数改进剂组合物的制备方法,其特征在于,所述的基础油为加氢精制基础油。
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