CN112480999B - 一种多功能导轨油 - Google Patents
一种多功能导轨油 Download PDFInfo
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Abstract
本发明公开了一种多功能导轨油,导轨油包括以下重量份数的原料:所述基础油40~60份、pH调节剂4~14份、聚醚多元醇衍生物5‑10份、缓蚀剂0.5~3.5份、杀菌剂1~5份、水2~10份。本发明的多功能导轨油同时能起到极压抗磨、减磨、抗乳化和消泡的功能,消除了传统导轨油和切削油由于添加剂不同而导致不能混用问题。
Description
技术领域
本发明属于化工技术领域,涉及一种导轨油,尤其涉及一种多功能导轨油。
背景技术
一般而言,导轨油主要应用于加工机床的导轨,要求具有良好的抗磨性和粘附性。在使用过程中,由于机床的往复切割而容易与切削油混合,形成污染,从而导致导轨油与切削油的功能失效,产生增加成本、降低生产效率等问题。
发明内容
本发明要解决的技术问题在于,针对现有技术的缺陷,提供一种同时能起到极压抗磨、减磨、抗乳化和消泡的功能,消除了传统导轨油和切削油由于添加剂不同而导致不能混用问题的多功能导轨油。
本发明解决其技术问题所采用的技术方案是:
一种多功能导轨油,其特征在于,包括以下重量份数的原料:
基础油 40~60
pH调节剂 4~14
聚醚多元醇衍生物 5~10
缓蚀剂 0.1~3.5
杀菌剂 1~5
水 2~10;
所述基础油为白油与油溶性聚醚的混合物、白油与2cSt的混合物或白油与4cSt的混合物;
所述的多功能导轨油中,优选R1为C1~C9的烷烃;R2为C1~C3的烷烃。
所述的多功能导轨油中,优选白油在40摄氏度的温度下的运动粘度为23-32mm2/s;油溶性聚醚在40摄氏度的温度下的运动粘度为23-32mm2/s。
所述的多功能导轨油中,优选所述pH调节剂为乙醇胺、二乙醇胺、三乙醇胺、AMP-95、CWT-03、氢氧化钾、氢氧化钠、吗啉、N-甲基吗啉、吡啶或碳酸钠。
所述的多功能导轨油中,优选所述缓蚀剂为苯骈三氮唑及其衍生物、甲基苯并三氮唑及其衍生物、巯基苯并三氮唑及其衍生物、烷基磷酸酯缓蚀剂、烷基磺酸盐、烷基琥珀酸盐、烷基羟乙基咪唑啉、羟基乙叉二膦酸、3,4-二甲基吡唑磷酸盐、亚硫酸钠、苯甲酸钠、环烷酸咪唑啉季铵盐、壬基酚聚氧乙烯醚中的一种或其复配物。
所述的多功能导轨油中,优选所述杀菌剂为MBM、BIT、BK、IPBC、893MW、LD14中的一种或其复配物。
一种聚醚多元醇衍生物的制备方法,包括以下步骤:
A、称取原料:环氧烷烃40-70份、起始剂40-50份,封端基团40-70份、4A分子筛催化剂,催化剂加入量为制得产物的20~40ppm(质量比);
B、将环氧烷烃加入到反应釜中,保持温度50-60℃温度下,以0.1~2mL/分钟的速率加入起始剂,添加完成后继续搅拌20-60min;
C、待压力达到常压时,将封端试剂添加到反应釜中,升温至60-100℃,老化0.5~3小时,得到聚醚多元醇衍生物。
本发明采用油溶性聚醚作为基础油的主要成分,聚醚多元醇衍生物作为主添加剂具有三方面优势:一、聚醚多元醇衍生物起到极压抗磨、减磨、抗乳化和消泡的功能,消除了传统产品中需要单独添加抗磨剂、减磨剂、抗乳化机以及消泡剂,降低了产品成本,提高了调和效率;二、油溶性聚醚与聚醚衍生物的结构相似,具有很好的相容性,不存在其他产品中会出现的分层、浑浊等现象;三、本发明产品既可以用于导轨润滑,又可以用于金属切割,消除了传统导轨油和切削油由于添加剂不同而导致不能混用的问题,减少油品污染带来的损失。还可以节约成本、提高生产效率。
具体实施方式
为了对本发明的技术特征、目的和效果有更加清楚的理解,现详细说明本发明的具体实施方式。
实施例1一种多功能导轨油,包括以下重量份数的原料:
所述基础油50份、pH调节剂乙醇胺4份、聚醚多元醇衍生物5份、缓蚀剂苯骈三氮唑0.5份、杀菌剂MBM 5份、水2份。
基础油为白油与油溶性聚醚的混合物;其中选择工业白油30份,油溶性聚醚20份,白油在40摄氏度的温度下的运动粘度为26.2mm2/s;油溶性聚醚在40摄氏度的温度下的运动粘度为25.0mm2/s。
多功能导轨油制备方法与现有导轨油制备方法基本相同。以下实施例不再赘述。
具体为:将基础油50份、pH调节剂乙醇胺4份、聚醚多元醇衍生物5份、缓蚀剂苯骈三氮唑0.5份、杀菌剂MBM 5份、水2份混合搅拌均匀,即得多功能导轨油。
本实施例的聚醚多元醇衍生物的制备方法,包括以下步骤:
A、称取原料:环氧烷烃40份、起始剂40份,封端基团40份、4A分子筛催化剂0.0024份;
B、将环氧烷烃加入到反应釜中,保持温度50℃温度下,以0.1mL/分钟的速率加入起始剂,添加完成后继续搅拌20min;
C、待压力达到常压时,将封端试剂添加到反应釜中,升温至60℃,老化0.5小时,得到聚醚多元醇衍生物。
实施例2、一种多功能导轨油,包括以下重量份数的原料:
所述基础油50份、pH调节剂二乙醇胺2份、聚醚多元醇衍生物7份、烷基磷酸酯缓蚀剂3.5份、杀菌剂MBM 4份、水2份。
基础油为白油与油溶性聚醚的混合物;其中选择工业白油30份,油溶性聚醚20份,白油在40摄氏度的温度下的运动粘度为25.2mm2/s;油溶性聚醚在40摄氏度的温度下的运动粘度为27.0mm2/s。
本实施例的聚醚多元醇衍生物的制备方法,包括以下步骤:
A、称取原料:环氧烷烃70份、起始剂50份,封端基团70份、4A分子筛催化剂0.0076份;
B、将环氧烷烃加入到反应釜中,保持温度60℃温度下,以2mL/分钟的速率加入起始剂,添加完成后继续搅拌60min;
C、待压力达到常压时,将封端试剂添加到反应釜中,升温至100℃,老化3小时,得到聚醚多元醇衍生物。
实施例3、一种多功能导轨油,包括以下重量份数的原料:
所述基础油50份、pH调节剂AMP-95 4份、聚醚多元醇衍生物10份、缓蚀剂甲基苯并三氮唑衍生物1.5份、杀菌剂IPBC 5份、水10份。
基础油为白油与油溶性聚醚的混合物;其中选择工业白油30份,油溶性聚醚20份,白油在40摄氏度的温度下的运动粘度为26.6mm2/s;油溶性聚醚在40摄氏度的温度下的运动粘度为30.0mm2/s。
本实施例的聚醚多元醇衍生物的制备方法,包括以下步骤:
A、称取原料:环氧烷烃50份、起始剂50份,封端基团50份、4A分子筛催化剂0.0045份;
B、将环氧烷烃加入到反应釜中,保持温度55℃温度下,以1mL/分钟的速率加入起始剂,添加完成后继续搅拌30min;
C、待压力达到常压时,将封端试剂添加到反应釜中,升温至70℃,老化2.5小时,得到聚醚多元醇衍生物。
实施例4、一种多功能导轨油,包括以下重量份数的原料:
所述基础油50份、pH调节剂(乙醇胺2份、二乙醇胺1份)、聚醚多元醇衍生物10份、缓蚀剂1.5份(苯骈三氮唑:甲基苯并三氮唑衍生物质量比为2:1)、杀菌剂BIT 4份、水8.5份。
基础油为白油与油溶性聚醚的混合物;其中选择工业白油30份,油溶性聚醚20份,白油在40摄氏度的温度下的运动粘度为26.4mm2/s;油溶性聚醚在40摄氏度的温度下的运动粘度为27.1mm2/s。
本实施例的聚醚多元醇衍生物的制备方法,包括以下步骤:
A、称取原料:环氧烷烃55份、起始剂50份,封端基团55份、4A分子筛催化剂0.0048份;
B、将环氧烷烃加入到反应釜中,保持温度55℃温度下,以0.5mL/分钟的速率加入起始剂,添加完成后继续搅拌40min;
C、待压力达到常压时,将封端试剂添加到反应釜中,升温至70℃,老化2.3小时,得到聚醚多元醇衍生物。
实施例5、一种多功能导轨油,包括以下重量份数的原料:
所述基础油50份、pH调节剂二乙醇胺3.5份、聚醚多元醇衍生物10份、缓蚀剂1.5份(苯骈三氮唑:甲基苯并三氮唑衍生物质量比为2:1)、杀菌剂BIT 2份、水8.5份。
基础油为白油与油溶性聚醚的混合物;其中选择工业白油30份,油溶性聚醚20份,白油在40摄氏度的温度下的运动粘度为27.2mm2/s;油溶性聚醚在40摄氏度的温度下的运动粘度为29.6mm2/s。
本实施例的聚醚多元醇衍生物的制备方法,包括以下步骤:
A、称取原料:环氧烷烃45份、起始剂45份,封端基团45份、4A分子筛催化剂0.0027份;
B、将环氧烷烃加入到反应釜中,保持温度60℃温度下,以1.5mL/分钟的速率加入起始剂,添加完成后继续搅拌30min;
C、待压力达到常压时,将封端试剂添加到反应釜中,升温至60℃,老化3小时,得到聚醚多元醇衍生物。
实施例6、一种多功能导轨油,包括以下重量份数的原料:
所述基础油50份、pH调节剂二乙醇胺1.5份、聚醚多元醇衍生物10份、缓蚀剂1.5份(苯骈三氮唑:甲基苯并三氮唑衍生物质量比为2:1)、杀菌剂BIT 3份、水6份。
基础油为白油与油溶性聚醚的混合物;其中选择工业白油30份,油溶性聚醚20份,白油在40摄氏度的温度下的运动粘度为26.4mm2/s;油溶性聚醚在40摄氏度的温度下的运动粘度为27.1mm2/s。
本实施例的聚醚多元醇衍生物的制备方法,包括以下步骤:
A、称取原料:环氧烷烃40份、起始剂40份,封端基团40份、4A分子筛催化剂0.0048份;
B、将环氧烷烃加入到反应釜中,保持温度70℃温度下,以1mL/分钟的速率加入起始剂,添加完成后继续搅拌40min;
C、待压力达到常压时,将封端试剂添加到反应釜中,升温至50℃,老化2.5小时,得到聚醚多元醇衍生物。
实施例7、一种多功能导轨油,包括以下重量份数的原料:
所述基础油60份、pH调节剂氢氧化钾14份、聚醚多元醇衍生物6份、缓蚀剂3,4-二甲基吡唑磷酸盐3.5份、杀菌剂LD14 3份、水5份。
基础油为白油与2cSt的混合物;其中选择工业白油40份,2cSt 20份,白油在40摄氏度的温度下的运动粘度为26.4mm2/s;油溶性聚醚在40摄氏度的温度下的运动粘度为7.4mm2/s。
本实施例的聚醚多元醇衍生物的制备方法,包括以下步骤:
A、称取原料:环氧烷烃55份、起始剂50份,封端基团55份、4A分子筛催化剂0.0048份;
B、将环氧烷烃加入到反应釜中,保持温度60℃温度下,以1.1mL/分钟的速率加入起始剂,添加完成后继续搅拌50min;
C、待压力达到常压时,将封端试剂添加到反应釜中,升温至65℃,老化2.3小时,得到聚醚多元醇衍生物。
实施例8、一种多功能导轨油,包括以下重量份数的原料:
所述基础油40份、pH调节剂吗啉10份、聚醚多元醇衍生物10份、缓蚀剂巯基苯并三氮唑0.2份、杀菌剂893MW 2.5份、水8份。
基础油为白油与4cSt的混合物;其中选择工业白油30份,4cSt 10份,白油在40摄氏度的温度下的运动粘度为26.4mm2/s;油溶性聚醚在40摄氏度的温度下的运动粘度为19.3mm2/s。
本实施例的聚醚多元醇衍生物的制备方法,包括以下步骤:
A、称取原料:环氧烷烃50份、起始剂50份,封端基团50份、4A分子筛催化剂0.0082份;
B、将环氧烷烃加入到反应釜中,保持温度60℃温度下,以1.6mL/分钟的速率加入起始剂,添加完成后继续搅拌55min;
C、待压力达到常压时,将封端试剂添加到反应釜中,升温至70℃,老化1.6小时,得到聚醚多元醇衍生物。
实施例9、一种多功能导轨油,包括以下重量份数的原料:
所述基础油40份、pH调节剂N-甲基吗啉11份、聚醚多元醇衍生物7份、缓蚀剂亚硫酸钠3.2份、杀菌剂893MW 2.7份、水6份。
基础油为白油与4cSt的混合物;其中选择工业白油25份,4cSt 15份,白油在40摄氏度的温度下的运动粘度为26.4mm2/s;油溶性聚醚在40摄氏度的温度下的运动粘度为19.3mm2/s。
本实施例的聚醚多元醇衍生物的制备方法,包括以下步骤:
A、称取原料:环氧烷烃60份、起始剂50份,封端基团60份、4A分子筛催化剂0.0034份;
B、将环氧烷烃加入到反应釜中,保持温度80℃温度下,以0.9mL/分钟的速率加入起始剂,添加完成后继续搅拌30min;
C、待压力达到常压时,将封端试剂添加到反应釜中,升温至70℃,老化3小时,得到聚醚多元醇衍生物。
实施例10、一种多功能导轨油,包括以下重量份数的原料:
所述基础油45份、pH调节剂碳酸钠13份、聚醚多元醇衍生物5份、缓蚀剂环烷酸咪唑啉季铵盐2.9份、杀菌剂IPBC 3份、水2份。
基础油为白油与4cSt的混合物;其中选择工业白油40份,4cSt 5份,白油在40摄氏度的温度下的运动粘度为26.4mm2/s;油溶性聚醚在40摄氏度的温度下的运动粘度为19.3mm2/s。
本实施例的聚醚多元醇衍生物的制备方法,包括以下步骤:
A、称取原料:环氧烷烃45份、起始剂45份,封端基团45份、4A分子筛催化剂0.0045份;
B、将环氧烷烃加入到反应釜中,保持温度55℃温度下,以2mL/分钟的速率加入起始剂,添加完成后继续搅拌30min;
C、待压力达到常压时,将封端试剂添加到反应釜中,升温至60℃,老化2.5小时,得到聚醚多元醇衍生物。
实施例11、一种多功能导轨油,包括以下重量份数的原料:
所述基础油50份、pH调节剂吡啶7份、聚醚多元醇衍生物7份、缓蚀剂烷基羟乙基咪唑啉2.6份、杀菌剂IPBC 3份、水6份。
基础油为白油与4cSt的混合物;其中选择工业白油35份,4cSt 15份,白油在40摄氏度的温度下的运动粘度为26.4mm2/s;油溶性聚醚在40摄氏度的温度下的运动粘度为19.3mm2/s。
本实施例的聚醚多元醇衍生物的制备方法,包括以下步骤:
A、称取原料:环氧烷烃55份、起始剂50份,封端基团55份、4A分子筛催化剂0.0039份;
B、将环氧烷烃加入到反应釜中,保持温度70℃温度下,以2mL/分钟的速率加入起始剂,添加完成后继续搅拌50min;
C、待压力达到常压时,将封端试剂添加到反应釜中,升温至65℃,老化1小时,得到聚醚多元醇衍生物。
实施例12、一种多功能导轨油,包括以下重量份数的原料:
所述基础油60份、pH调节剂CWT-03 12份、聚醚多元醇衍生物8份、缓蚀剂壬基酚聚氧乙烯醚3.4份、杀菌剂BK 4份、水8份。
基础油为白油与4cSt的混合物;其中选择工业白油35份,4cSt 25份,白油在40摄氏度的温度下的运动粘度为26.4mm2/s;油溶性聚醚在40摄氏度的温度下的运动粘度为19.3mm2/s。
本实施例的聚醚多元醇衍生物的制备方法,包括以下步骤:
A、称取原料:环氧烷烃60份、起始剂50份,封端基团60份、4A分子筛催化剂0.0068份;
B、将环氧烷烃加入到反应釜中,保持温度40℃温度下,以0.6mL/分钟的速率加入起始剂,添加完成后继续搅拌60min;
C、待压力达到常压时,将封端试剂添加到反应釜中,升温至88℃,老化1.5小时,得到聚醚多元醇衍生物。
对比实验:
对比例1:
水溶性切削液:市售某著名品牌水溶液;
对比例2:
导轨油:市售某著名品牌ISO VG 68#导轨油;
将实施例1-12、对比例1、对比例2加水配制成5%稀释液,性能如表1、表2所示。
表1实施例与对比例应用效果对比(切削性能)
从表1可以看出:相比于对比例,实施例产品对铜片、铝片、铁片和T3铜片具有优异的防腐蚀性能,具有较高的PB值,摩擦系数优异,磨斑直径较小,说明了本发明产品中的聚醚多元醇衍生物发挥了作用。
在导轨油的应用方面,本实施例产品与对比产品的性能进行比较,结果发现,本发明实施例产品与对比例产品在相同的加工时间内,没有发现有表面浮油,经过培养后的菌落数较低,且机台工作表面清洁,体现出本发明产品的抗菌性好、溶解性强以及易于清洁等特点。
表2实施例与对比例应用效果对比(导轨性能)
Claims (6)
1.一种多功能导轨油,其特征在于,由以下重量份数的原料制成:
基础油40~60
pH调节剂4~14
聚醚多元醇衍生物5~10
缓蚀剂0.1~3.5
杀菌剂1~5
水2~10;
所述基础油为白油与油溶性聚醚的混合物、白油与2 cSt的混合物或白油与4 cSt的混合物;
2.根据权利要求1所述的多功能导轨油,其特征在于,R1为C1~C9的烷烃;R2为C1~C3的烷烃。
3.根据权利要求1所述的多功能导轨油,其特征在于,白油在40摄氏度的温度下的运动粘度为23-32mm2/s;油溶性聚醚在40摄氏度的温度下的运动粘度为23-32mm2/s。
4.根据权利要求1所述的多功能导轨油,其特征在于,所述pH调节剂为乙醇胺、二乙醇胺、三乙醇胺、AMP-95、CWT-03、氢氧化钾、氢氧化钠、吗啉、N-甲基吗啉、吡啶或碳酸钠。
5.根据权利要求1所述的多功能导轨油,其特征在于,所述缓蚀剂为苯骈三氮唑及其衍生物、甲基苯并三氮唑及其衍生物、巯基苯并三氮唑及其衍生物烷基、磷酸酯缓蚀剂、烷基磺酸盐、烷基琥珀酸盐、烷基羟乙基咪唑啉、羟基乙叉二膦酸、3,4-二甲基吡唑磷酸盐、亚硫酸钠、苯甲酸钠、环烷酸咪唑啉季铵盐、壬基酚聚氧乙烯醚中的一种或其复配物。
6.根据权利要求1所述的多功能导轨油,其特征在于,所述杀菌剂为MBM、BIT、BK、IPBC、893MW、LD14中的一种或其复配物。
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