CN1098345C - Antioxidative succinimide dustless dispersing agent - Google Patents
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本发明涉及一种油品添加剂,确切地说是一种用于内燃机油或燃料油的具有抗氧化性能的丁二酰亚胺无灰分散剂。The invention relates to an oil additive, specifically a succinimide ashless dispersant with oxidation resistance for internal combustion engine oil or fuel oil.
丁二酰亚胺分散剂于60年代就开始大量使用,目前仍是应用最广和用量最大的一种分散剂,其制备方法是:先由分子量1000-3000的聚异丁烯与马来酸酐反应,生成聚异丁烯基马来酸酐,然后再与不同比例的多烯多胺反应,制得单、双和多聚异丁烯基丁二酰亚胺。The succinimide dispersant has been widely used since the 1960s, and it is still the most widely used and the largest amount of dispersant. Its preparation method is: first react polyisobutylene with a molecular weight of 1000-3000 and maleic anhydride, Generate polyisobutenyl maleic anhydride, and then react with different proportions of polyene polyamines to obtain mono-, di-, and polyisobutenyl succinimides.
由于发动机的操作温度范围很宽,在冬季停停开开的操作条件下,汽车曲轴箱的温度低,燃料烃和湿气(水份)不易从润滑油中排出,导致发动机油产生大量的油泥,影响发动机的正常运转;夏季,连续驾驶导致操作温度升高,内燃机油易发生氧化,使粘度迅速增长,活塞上积炭和漆膜增加。为此,要求内燃机油既要有很好的低温油泥分散性,又要求具有优良的高温抗氧化能力。Due to the wide operating temperature range of the engine, under the operating conditions of stop and go in winter, the temperature of the crankcase of the car is low, and the fuel hydrocarbons and moisture (moisture) are not easily discharged from the lubricating oil, resulting in a large amount of sludge in the engine oil , affecting the normal operation of the engine; in summer, continuous driving causes the operating temperature to rise, and the internal combustion engine oil is prone to oxidation, which causes the viscosity to increase rapidly, and the carbon deposit and paint film on the piston increase. Therefore, internal combustion engine oil is required to have good low-temperature sludge dispersibility and excellent high-temperature oxidation resistance.
US 4973412公开了一种多功能的润滑油添加剂,其制备方法是:先用有机二元酸偶联部分酰化的丁二酰亚胺,再用不饱和脂肪酸处理,最后再与具有抗氧化性能的亚硝基对苯二胺反应即得。该添加剂改进了丁二酰亚胺的抗氧化性能,但其制备工艺比较复杂。US 4973412 discloses a multifunctional lubricating oil additive. Its preparation method is: first use organic dibasic acid coupling partially acylated succinimide, then treat it with unsaturated fatty acid, and finally combine it with The reaction of nitroso-p-phenylenediamine can be obtained. The additive improves the oxidation resistance of succinimide, but its preparation process is relatively complicated.
US 4636322、4699724、4713189公开了偶联的丁二酰亚胺分散剂,是由苯酚、双酚A、间苯二酚、单壬基酚或β-萘酚通过曼尼希反应偶联丁二酰亚胺,再用羟基乙酸酰化部分多烯多胺制备而成。该添加剂改善了分散性和对橡胶密封圈的适应性,但没有提及改善氧化安定性问题。US 4636322, 4699724, 4713189 disclose coupled succinimide dispersants, which are made of phenol, bisphenol A, resorcinol, monononylphenol or β-naphthol through Mannich reaction coupling butanedi The imide is prepared by acylation of part of the polyene polyamine with glycolic acid. This additive improves dispersibility and adaptability to rubber seals, but does not mention improving oxidation stability.
本发明的目的是提供一种与已有技术结构不同的既能改善低温分散性能,又能增强抗氧化性能的丁二酰亚胺型无灰分散剂。The purpose of the present invention is to provide a succinimide type ashless dispersant which is different from the structure of the prior art and can not only improve the low-temperature dispersion performance but also enhance the oxidation resistance.
本发明提供的抗氧性丁二酰亚胺无灰分散剂结构上含有如下基团:烯基丁二酰基,酚偶联的多烯多胺基,与多烯多胺基相连的2,6-二叔丁基酚基。该分散剂是按如下方法制备的:The antioxidant succinimide ashless dispersant provided by the present invention contains the following groups in structure: alkenyl succinyl group, polyene polyamine group coupled with phenol, 2,6- Di-tert-butylphenol. The dispersant is prepared as follows:
(1)在2,6-二叔丁基酚的存在下,将含αH的酚、多烯多胺和甲醛混(1) In the presence of 2,6-di-tert-butylphenol, mix αH-containing phenol, polyene polyamine and formaldehyde
合,进行曼尼希反应,分离产物,制得中间产品缩合胺;Combine, carry out Mannich reaction, separate product, make intermediate product condensed amine;
(2)将烯基丁二酸酐与上述缩合胺进行胺化反应,得到最终产品。(2) Alkenyl succinic anhydride and the above-mentioned condensed amine are subjected to amination reaction to obtain the final product.
具体地说,本发明提供的分散剂可以按如下方法制备:Specifically, the dispersant provided by the invention can be prepared as follows:
(1)在氮气保护下,将2,6-二叔丁基酚、含αH的酚、多烯多胺和甲醛混合,在搅拌下缓慢升温,在室温~150℃,优选60~120℃下反应1~10小时,优选2~8小时,减压蒸馏脱除水和未反应的物质,得到偶联的含抗氧基团的多烯多胺,即缩合胺。(1) Under the protection of nitrogen, mix 2,6-di-tert-butylphenol, phenol containing αH, polyene polyamine and formaldehyde, slowly heat up under stirring, at room temperature ~ 150 ° C, preferably 60 ~ 120 ° C React for 1 to 10 hours, preferably 2 to 8 hours, and distill under reduced pressure to remove water and unreacted substances to obtain a coupled polyene polyamine containing antioxidant groups, that is, condensed amine.
其中,含αH的酚可以选自苯酚、对甲酚、对苯二酚、双酚A或β-萘酚之一,也可以是其中二种或二种以上的混合物,含αH的酚与多烯多胺的摩尔比为1∶1~4,含αH的酚与2,6-二叔丁基酚的摩尔比为1∶0.2~3,优选1∶0.5~2,这两种酚可以与甲醛和多烯多胺同时加入反应器,也可以后加入,加入的温度以不超70℃为宜。Wherein, the phenol containing αH can be selected from one of phenol, p-cresol, hydroquinone, bisphenol A or β-naphthol, or a mixture of two or more thereof. The molar ratio of polyamine is 1: 1~4, the molar ratio of the phenol containing αH and 2,6-di-tert-butylphenol is 1: 0.2~3, preferably 1: 0.5~2, these two kinds of phenols can be combined with Formaldehyde and polyene polyamine are added to the reactor at the same time, or they can be added later, and the temperature of addition should not exceed 70°C.
所说多烯多胺的通式为H2N(CH2CH2NH)nH,式中n为1~6的整数,如乙二胺(EDA)、二乙烯三胺(DETA)、三乙烯四胺(TETA)、四乙烯五胺(TEPA)、五乙烯六胺(DEHA)等。The general formula of said polyene polyamine is H 2 N(CH 2 CH 2 NH) n H, where n is an integer of 1 to 6, such as ethylenediamine (EDA), diethylenetriamine (DETA), tri Ethylenetetramine (TETA), tetraethylenepentamine (TEPA), pentaethylenehexamine (DEHA), etc.
所说甲醛可以是受热后可以分解为甲醛的多聚甲醛;也可以是甲醛水溶液,最好是浓度为36重%的甲醛饱和水溶液。如果是多聚甲醛,则可以与其它反应物同时混合;如果是甲醛水溶液,则最好是先将其它反应物混合后,再将甲醛水溶液逐步滴入。甲醛的用量应适当过量,最好是含αH的酚和2,6-二叔丁基酚中具有反应活性的H的总和的1~2倍。Said formaldehyde can be paraformaldehyde that can be decomposed into formaldehyde after being heated; it can also be an aqueous solution of formaldehyde, preferably a saturated aqueous solution of formaldehyde with a concentration of 36% by weight. If it is paraformaldehyde, it can be mixed with other reactants at the same time; if it is a formaldehyde solution, it is best to mix other reactants first, and then gradually add the formaldehyde solution. The amount of formaldehyde should be in excess, preferably 1 to 2 times the sum of reactive H in αH-containing phenol and 2,6-di-tert-butylphenol.
该步骤制得的缩合胺的结构中,含αH的酚根据其所含具有反应活性的H的数量,可以与1~4个多烯多胺相连,可以连在伯氨基上,也可以连在仲氨基上。例如,苯酚不仅有两个邻位H,还有一个对位H也可参与反应,因此有三个具有反应活性的H。2,6-二叔丁基酚的对位上,可以与一个多烯多胺相连,同样可以连在伯氨基上,也可以连在仲氨基上。含αH的酚与2,6-二叔丁基酚在产物结构中的相对含量视投料比而定。In the structure of the condensed amine prepared in this step, the phenol containing αH can be connected with 1 to 4 polyene polyamines according to the amount of reactive H contained in it, and can be connected with primary amino groups or with on the secondary amino group. For example, phenol not only has two ortho Hs, but also has a para H that can also participate in the reaction, so there are three reactive Hs. The para-position of 2,6-di-tert-butylphenol can be connected with a polyene polyamine, also can be connected with the primary amino group, and also can be connected with the secondary amino group. The relative content of αH-containing phenol and 2,6-di-tert-butylphenol in the product structure depends on the feed ratio.
(2)在稀释油和氮气存在下,将步骤(1)制得的缩合胺与烯基丁二酸酐在60~160℃,优选80~140℃反应1~8小时,优选2~6小时,减压脱除反应生成的水,过滤,得最终产品无灰分散剂。其中烯基丁二酸酐的加入量为步骤(1)中多烯多胺摩尔数的0.6~3倍,优选0.7~2.5倍。另外,为了便于反应平稳进行,可以在氮气保护下,先将烯基丁二酸酐溶解在稀释油中,加热至60~90℃,再缓慢加入缩合胺进行反应。(2) In the presence of diluent oil and nitrogen, the condensed amine prepared in step (1) is reacted with alkenyl succinic anhydride at 60 to 160° C., preferably 80 to 140° C., for 1 to 8 hours, preferably 2 to 6 hours, Remove the water generated by the reaction under reduced pressure, and filter to obtain the final ashless dispersant. The amount of alkenyl succinic anhydride added is 0.6 to 3 times, preferably 0.7 to 2.5 times, the molar number of polyene polyamine in step (1). In addition, in order to facilitate the smooth progress of the reaction, alkenyl succinic anhydride can be dissolved in diluent oil under the protection of nitrogen, heated to 60-90°C, and then slowly added condensed amine for reaction.
所说烯基丁二酸酐中的烯基为C2~C10的烯烃共聚物或均聚物,最好是聚异丁烯。烯基的数均分子量可以为500~5000,优选900~2500,分子量分布一般为1.5~4.5,优选1.5~3.5。The alkenyl in said alkenyl succinic anhydride is a C 2 -C 10 olefin copolymer or homopolymer, preferably polyisobutylene. The number average molecular weight of the alkenyl group can be 500-5000, preferably 900-2500, and the molecular weight distribution is generally 1.5-4.5, preferably 1.5-3.5.
在生成终产物时,烯基丁二酸酐可以连在一个伯氨基上,形成酰亚胺;也可以开环后连在两个仲氨基上,形成酰胺。烯基丁二酸酐是用长链烯烃聚合物与马来酸酐进行烃化反应制得,可自制,也可从市场购买。When generating the final product, alkenyl succinic anhydride can be connected to a primary amino group to form an imide; it can also be connected to two secondary amino groups after ring opening to form an amide. Alkenyl succinic anhydride is prepared by alkylating long-chain olefin polymers with maleic anhydride, and can be made by yourself or purchased from the market.
本发明提供的无灰分散剂在引入抗氧基团的同时将多烯多胺偶联,提高了氮含量,因此不仅具有了良好的高温抗氧性能,还改善了分散性能,而且能保证良好的油溶性。The ashless dispersant provided by the present invention couples polyene polyamines while introducing anti-oxygen groups to increase nitrogen content, so it not only has good high-temperature anti-oxidation performance, but also improves dispersion performance, and can ensure good oil soluble.
下面通过实施例对本发明作进一步说明。Below by embodiment the present invention will be further described.
实施例1~8为缩合胺中间体的制备。Embodiments 1-8 are the preparation of condensed amine intermediates.
实施例1Example 1
在带有机械搅拌、控温热电偶和温度计的250ml的三口瓶中,加入56.8g(0.3mol)四乙烯五胺,和16.5g多聚甲醛,在氮气保护下,加热至90℃,保持1h,冷却至65℃加入20.6g(0.1mol)2,6-二叔丁基酚和9.4g(0.1mol)苯酚,保持0.5h,缓慢加热至120℃,保持3h,减压蒸馏脱除水和未反应的物质,制得的缩合胺中间体A。Add 56.8g (0.3mol) of tetraethylenepentamine and 16.5g of paraformaldehyde into a 250ml three-neck flask with mechanical stirring, temperature control thermocouple and thermometer, and heat to 90°C under nitrogen protection for 1h , cooled to 65°C, added 20.6g (0.1mol) 2,6-di-tert-butylphenol and 9.4g (0.1mol) phenol, kept for 0.5h, slowly heated to 120°C, kept for 3h, decompressed distillation to remove water and Unreacted material, condensed amine intermediate A prepared.
实施例2Example 2
在带有机械搅拌、控温热电偶和温度计的250ml的三口瓶中,加入56.8g(0.3mol)四乙烯五胺,9.4g(0.1mol)苯酚,20.6g(0.1mol)2,6-二叔丁基酚和15g多聚甲醛,在氮气保护下,缓慢加热至90℃,保持2h后继续加热至110℃保持2h,减压蒸馏脱除水和未反应的物质,制得的缩合胺中间体B。In a 250ml three-neck flask with mechanical stirring, temperature control thermocouple and thermometer, add 56.8g (0.3mol) tetraethylenepentamine, 9.4g (0.1mol) phenol, 20.6g (0.1mol) 2,6-di tert-butylphenol and 15g paraformaldehyde, under the protection of nitrogen, slowly heated to 90°C, kept for 2h, then continued to heat to 110°C, kept for 2h, decompressed distillation to remove water and unreacted substances, and the condensed amine intermediate prepared Body B.
实施例3Example 3
在带有机械搅拌、控温热电偶和温度计的250ml的三口瓶中,加入38.0g(0.2mol)四乙烯五胺和12.0g多聚甲醛,在氮气保护下,加热至65℃,保持1小时,加入10.3g(0.05mol)2,6-二叔丁基酚(0.1mol)和9.4g(0.1mol)苯酚,保持1h,缓慢加热至120℃,保持1h,减压蒸馏脱除水和未反应的物质,制得的缩合胺中间体C。In a 250ml three-neck flask equipped with mechanical stirring, temperature control thermocouple and thermometer, add 38.0g (0.2mol) tetraethylenepentamine and 12.0g paraformaldehyde, under the protection of nitrogen, heat to 65°C and keep for 1 hour , add 10.3g (0.05mol) 2,6-di-tert-butylphenol (0.1mol) and 9.4g (0.1mol) phenol, keep for 1h, slowly heat to 120°C, keep for 1h, distill under reduced pressure to remove water and unused The substance of the reaction, the condensed amine intermediate C obtained.
实施例4Example 4
在带有机械搅拌、控温热电偶和温度计的250ml的三口瓶中,加入56.8g(0.3mol)四乙烯五胺,9.4g(0.1mol)苯酚,41.2g(0.2mol)2,6-二叔丁基酚和和19g多聚甲醛,在氮气保护下,缓慢加热至90℃,保持2h后继续加热至110℃保持2h,减压蒸馏脱除水和未反应的物质,制得的缩合胺中间体D。In a 250ml three-neck flask with mechanical stirring, temperature control thermocouple and thermometer, add 56.8g (0.3mol) tetraethylenepentamine, 9.4g (0.1mol) phenol, 41.2g (0.2mol) 2,6-di tert-butylphenol and 19g of paraformaldehyde, under the protection of nitrogen, slowly heated to 90°C, kept for 2h, then continued to heat to 110°C for 2h, distilled under reduced pressure to remove water and unreacted substances, the obtained condensed amine Intermediate D.
实施例5Example 5
在带有机械搅拌、控温热电偶和温度计的250ml的三口瓶中,加入73g(0.5mol)三乙烯四胺,9.4g(0.1mol)苯酚,61.8g(0.3mol)2,6-二叔丁基酚,在氮气保护下,逐渐加入42ml甲醛溶液,然后,加热至100℃,回流4h后,减压蒸馏脱除水和未反应的物质,制得的缩合胺中间体E。In a 250ml three-neck flask with mechanical stirring, temperature control thermocouple and thermometer, add 73g (0.5mol) triethylenetetramine, 9.4g (0.1mol) phenol, 61.8g (0.3mol) 2,6-ditertiary Butylphenol, under the protection of nitrogen, gradually added 42ml of formaldehyde solution, then heated to 100°C, refluxed for 4 hours, and distilled under reduced pressure to remove water and unreacted substances to obtain the condensed amine intermediate E.
实施例6Example 6
在带有机械搅拌、控温热电偶和温度计的250ml的三口瓶中,加入75.7g(0.4mol)四乙烯五胺,9.4g(0.1mol)苯酚,30.9g(0.15mol)2,6-二叔丁基酚和15g多聚甲醛,在氮气保护下,缓慢加热至90℃,保持2h后继续加热至110℃保持2h,减压蒸馏脱除水和未反应的物质,制得的缩合胺中间体F。In a 250ml three-neck flask with mechanical stirring, temperature control thermocouple and thermometer, add 75.7g (0.4mol) tetraethylenepentamine, 9.4g (0.1mol) phenol, 30.9g (0.15mol) 2,6-di tert-butylphenol and 15g paraformaldehyde, under the protection of nitrogen, slowly heated to 90°C, kept for 2h, then continued to heat to 110°C, kept for 2h, decompressed distillation to remove water and unreacted substances, and the condensed amine intermediate prepared Body F.
实施例7Example 7
在带有机械搅拌、控温热电偶和温度计的250ml的三口瓶中,加入38.2g(0.2mol)四乙烯五胺,10.9g(0.1mol)对甲酚,20.6g(0.1mol)2,6-二叔丁基酚,在氮气保护下,逐渐滴入32ml甲醛水溶液,缓慢加热至100℃,回流4h后减压蒸馏脱除水和未反应的物质,制得的缩合胺中间体G。In a 250ml three-neck flask with mechanical stirring, temperature control thermocouple and thermometer, add 38.2g (0.2mol) tetraethylenepentamine, 10.9g (0.1mol) p-cresol, 20.6g (0.1mol) 2,6 - Di-tert-butylphenol, under the protection of nitrogen, gradually drop 32ml of aqueous formaldehyde solution, slowly heat to 100°C, reflux for 4 hours, and then distill off water and unreacted substances under reduced pressure to obtain the condensed amine intermediate G.
实施例8Example 8
在带有机械搅拌、控温热电偶和温度计的250ml的三口瓶中,加入79.5(0.42mol)g四乙烯五胺,22.2g(0.1mol)双酚A,30.2g(0.15mol)2,6-二叔丁基酚,在氮气保护下,逐渐滴入32ml甲醛水溶液,缓慢加热至100℃,回流2h,减压蒸馏脱除水和未反应的物质,制得的缩合胺中间体H。In a 250ml three-neck flask with mechanical stirring, temperature control thermocouple and thermometer, add 79.5 (0.42mol) g tetraethylenepentamine, 22.2g (0.1mol) bisphenol A, 30.2g (0.15mol) 2,6 -Di-tert-butylphenol, under the protection of nitrogen, gradually drop 32ml of aqueous formaldehyde solution, slowly heat to 100°C, reflux for 2h, and distill under reduced pressure to remove water and unreacted substances to obtain the condensed amine intermediate H.
实施例9~16为抗氧性丁二酰亚胺无灰分散剂的制备。Examples 9-16 are preparations of anti-oxidant succinimide ashless dispersants.
实施例9Example 9
在带有机械搅拌、控温热电偶和温度计的250ml的三口瓶中,加入50g烯基丁二酸酐(聚异丁烯的分子量为2300)和50g150SN稀释油,氮气保护下加热至85℃,加入实施例1中的缩合胺中间体A 5.1g,保持1h,升温140℃,保持2h,真空脱水1h,经过滤得最终的无灰分散剂。In a 250ml three-neck flask with mechanical stirring, temperature control thermocouple and thermometer, add 50g of alkenyl succinic anhydride (the molecular weight of polyisobutylene is 2300) and 50g of 150SN diluent oil, heat to 85°C under nitrogen protection, add the example 5.1g of condensed amine intermediate A in 1, keep for 1h, raise the temperature to 140°C, keep for 2h, vacuum dehydrate for 1h, and filter to get the final ashless dispersant.
实施例10Example 10
胺化条件同实施例9,以实施例2中的缩合胺B代替缩合胺A,使烯酐与缩合胺(相当于四乙烯五胺)的摩尔比为1.5∶1,制得无灰分散剂,其性能评定见表1。The amination conditions are the same as in Example 9, and the condensed amine B in Example 2 is used instead of the condensed amine A, so that the molar ratio of the alkene anhydride to the condensed amine (equivalent to tetraethylenepentamine) is 1.5:1, and an ashless dispersant is obtained. Its performance evaluation is shown in Table 1.
实施例11Example 11
胺化条件同实施例9,以实施例3中相同摩尔数的缩合胺C代替缩合胺A,制得无灰分散剂,性能评定见表1。The amination conditions were the same as in Example 9, and the condensed amine C with the same molar number as in Example 3 was used instead of the condensed amine A to prepare an ashless dispersant. See Table 1 for performance evaluation.
实施例12Example 12
胺化条件同实施例9,以实施例4中相同摩尔数的缩合胺D代替缩合胺A,采用聚异丁烯分子量为900的烯酐,制得无灰分散剂,性能评定见表1。The amination conditions were the same as in Example 9, and the condensed amine D was replaced by the condensed amine A with the same molar number in Example 4, and polyisobutylene alkene anhydride with a molecular weight of 900 was used to prepare an ashless dispersant. The performance evaluation is shown in Table 1.
实施例13Example 13
胺化条件同实施例9,以实施例5中相同摩尔数的缩合胺E代替缩合胺A,制得无灰分散剂,其性能评定见表1。The amination conditions were the same as in Example 9, and the condensed amine E with the same molar number as in Example 5 was used instead of the condensed amine A to obtain an ashless dispersant, and its performance evaluation is shown in Table 1.
实施例14Example 14
胺化条件同实施例9,以实施例6中相同摩尔数的缩合胺F代替缩合胺A,制得无灰分散剂,其性能评定见表1。The amination conditions were the same as in Example 9, and the condensed amine F with the same molar number as in Example 6 was used instead of the condensed amine A to obtain an ashless dispersant, and its performance evaluation is shown in Table 1.
实施例15Example 15
胺化条件同实施例9,以实施例7中相同摩尔数的缩合胺G代替缩合胺A,采用聚异丁烯分子量为1300的烯酐,制得无灰分散剂,性能评定见表1。The amination conditions were the same as in Example 9, and the condensed amine G with the same molar number as in Example 7 was used to replace the condensed amine A, and polyisobutylene alkene anhydride with a molecular weight of 1300 was used to prepare an ashless dispersant. The performance evaluation is shown in Table 1.
实施例16Example 16
胺化条件同实施例9,以实施例8中的缩合胺F代替缩合胺A,使烯酐与缩合胺(相当于四乙烯五胺)的摩尔比为0.78∶1,制得无灰分散剂,其性能评定见表1。The amination conditions are the same as in Example 9, and the condensed amine F in Example 8 is used to replace the condensed amine A, so that the molar ratio of the alkene anhydride to the condensed amine (equivalent to tetraethylenepentamine) is 0.78:1, and an ashless dispersant is obtained. Its performance evaluation is shown in Table 1.
对比例1Comparative example 1
本对比例为普通单挂无灰分散剂的制备。This comparative example is the preparation of a common single-hanging ashless dispersant.
按照实施例9的反应条件,将5.1克缩合胺改为3.2克四乙烯五胺,制得普通单挂无灰分散剂,其性能评定见表1。According to the reaction conditions of Example 9, 5.1 g of condensed amine was changed to 3.2 g of tetraethylenepentamine to obtain a common single-hanging ashless dispersant, and its performance evaluation is shown in Table 1.
对比例2Comparative example 2
本对比例为普通双挂无灰分散剂的制备。This comparative example is the preparation of a common double-hanging ashless dispersant.
按照实施例9的反应条件,将5.1克缩合胺改为1.7克四乙烯五胺,制得普通双挂无灰分散剂。其性能评定见表1。According to the reaction conditions in Example 9, 5.1 g of condensed amine was changed to 1.7 g of tetraethylenepentamine to prepare a common double-hung ashless dispersant. Its performance evaluation is shown in Table 1.
实施例17Example 17
本实施例为分散性能评定。This example is for the evaluation of dispersion performance.
采用逆流粘度增长法,用碳黑作烟炱模拟物,分散到含0.5%分散剂的150SN基础油中,碳黑用量为1%,测定粘度增长率,增长率小的分散性好。测试结果见表1。Using countercurrent viscosity growth method, carbon black is used as soot simulant, dispersed in 150SN base oil containing 0.5% dispersant, and the amount of carbon black is 1%, the viscosity growth rate is measured, and the dispersion with small growth rate is better. The test results are shown in Table 1.
实施例18Example 18
本实施例为抗氧性能评定。This example is for the evaluation of anti-oxidation performance.
采用PDSC压力差示扫描量热仪测定添加剂的氧化诱导期,该值越大说明抗氧性能越好。测试条件为:美国DuPont2100仪器,O2气氛下,压力5kg/cm2,恒温220℃,样品量2mg。测试结果见表1。The PDSC pressure differential scanning calorimeter was used to measure the oxidation induction period of the additive, and the larger the value, the better the antioxidant performance. The test conditions are: American DuPont2100 instrument, O 2 atmosphere, pressure 5kg/cm 2 , constant temperature 220°C, sample size 2mg. The test results are shown in Table 1.
从表1可以看出,本发明提供的抗氧性丁二酰亚胺无灰分散剂与普通单挂和双挂无灰分散剂相比,不仅具有了抗氧性能,还改善了分散性能。It can be seen from Table 1 that the antioxidant succinimide ashless dispersant provided by the present invention not only has anti-oxidation performance but also improves dispersion performance compared with common single-hung and double-hung ashless dispersants.
表1
Claims (9)
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| US20080040968A1 (en) * | 2006-08-17 | 2008-02-21 | Malfer Dennis J | Fuel additive compounds and method of making the compounds |
| CN103374454B (en) * | 2012-04-26 | 2015-10-28 | 中国石油化工股份有限公司 | Gas engine oil compositions and manufacture method thereof |
| CN114507301B (en) * | 2020-10-28 | 2023-12-12 | 中国石油化工股份有限公司 | Method and system for producing polyisobutene succinimide ashless dispersant |
| CN118146858A (en) * | 2022-12-07 | 2024-06-07 | 中国石油天然气股份有限公司 | Environmentally friendly water turbine lubricating oil composition |
| CN119264963B (en) * | 2023-07-04 | 2025-11-25 | 中国石油天然气股份有限公司 | A Mannich ashless dispersant, a lubricating oil composition and its application |
Citations (4)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| US4636322A (en) * | 1985-11-04 | 1987-01-13 | Texaco Inc. | Lubricating oil dispersant and viton seal additives |
| US4699724A (en) * | 1986-08-20 | 1987-10-13 | Texaco Inc. | Post-coupled mono-succinimide lubricating oil dispersant and viton seal additives |
| US4713189A (en) * | 1986-08-20 | 1987-12-15 | Texaco, Inc. | Precoupled mono-succinimide lubricating oil dispersants and viton seal additives |
| US4973412A (en) * | 1990-05-07 | 1990-11-27 | Texaco Inc. | Multifunctional lubricant additive with Viton seal capability |
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| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| US4636322A (en) * | 1985-11-04 | 1987-01-13 | Texaco Inc. | Lubricating oil dispersant and viton seal additives |
| US4699724A (en) * | 1986-08-20 | 1987-10-13 | Texaco Inc. | Post-coupled mono-succinimide lubricating oil dispersant and viton seal additives |
| US4713189A (en) * | 1986-08-20 | 1987-12-15 | Texaco, Inc. | Precoupled mono-succinimide lubricating oil dispersants and viton seal additives |
| US4973412A (en) * | 1990-05-07 | 1990-11-27 | Texaco Inc. | Multifunctional lubricant additive with Viton seal capability |
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