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process for preparing a stable dispersion of barium carbonate, which can be used as an additive for lubricating oils

机译:碳酸钡稳定分散体的制备方法,该碳酸钡可用作润滑油的添加剂

摘要

A lubricating oil composition may contain 1 to 20% of a dispersion of a barium carbonate material, 0.65 to 7% of oil-compatible oxidation inhibitors and antifoaming agents and sufficient oil base to make 100%, all percentages being by weight. The lubricating oil base is preferably a blend of high viscosity, highly refined mineral lubricating oils. The finished oil composition should have a base number of at least about 2.0 and preferably not less than about 3. A four point depressant and viscosity index improver may be added. The specified oxidation inhibitor is zinc dithiophosphate, and the foam inhibitor is silicone oil.ALSO:A barium-carbonate-containing dispersion is produced by forming a mixture containing an oil-soluble dispersing agent, a non-volatile, oil-soluble, diluent liquid, a glycol ether solution of barium oxide and/or hydroxide-said solution having a base number of at least 110 and the ether having the formula R.O.CH2.CH2.OH, or R1.O.CH2.CH2.O.CH2.CH2.OH where R is a hydrocarbon group containing 1-6 carbon atoms and R1 is a hydrocarbon group containing 1 to 4 carbon atoms-and passing CO2 through the mixture to produce the desired dispersed material and removing undesired volatile material either before or after the carbonation step by steam treatment or boiling to produce the desired dispersion. Preferred dispersing agents are oil-soluble sulphonic acids, carboxylic acids or phosphorus sulphide treated olefines and metal salts thereof. The oil soluble diluent liquid is preferably a mineral or synthetic lubricating oil. 1 to 5 moles of CO2 may be passed through the mixture for each mole of a neutralized barium containing base present therein. A preferred composition of the reaction mixture is given, and the preferred ether is 2-methoxy-ethanol. The mixing may be carried out at atmospheric pressure at a temperature of 25-120 DEG C. and the CO2 may be bubbled through the mixture at a temperature of 21-63 DEG C. until it is acidic to p-naphthol benzein indicator.ALSO:A solution comprises a glycol ether having the formula R.O.CH2OH or R1O.CH2.CH2. O.CH2.CH2.OH, where R is a hydrocarbon group containing 1 to 6 carbon atoms and R1 is a hydrocarbon group containing from 1-4 carbon atoms which ether has in solution at least 18.5% by weight of Ba calculated as carbonate. The solution may be prepared by adding Ba oxide and/or hydroxide to the glycol ether preferably in small increments so as to avoid excessive heating of the mixture as a result of the exothermic reaction which occurs. The addition is also preferably made under a blanket of inert gas e.g. N2 in the presence of small amount of oxidation inhibiting compoun e.g. ditertiary butyl cresol in amount of 0.025 to 0.1% by weight. If it is desired to add the whole of the barium base at once, the mixture must be cooled to keep the temperature below the b.pt. of the glycol, e.g. at a temperature from 80-90 DEG C. After the reacation has subsided, the mixture is heated to a temperature between 80 DEG C. and the b.pt. of the glycol for a period of 10-30 minutes and then cooled. In the examples the ether used is 2-methoxy ethanol.
机译:润滑油组合物可包含1至20%的碳酸钡材料的分散体,0.65至7%的油相容性抗氧化剂和消泡剂以及足以制成100%的油基,所有百分比均以重量计。润滑油基料优选是高粘度,高度精炼的矿物润滑油的混合物。成品油组合物的碱值应至少为约2.0,优选不小于约3。可以加入四点抑制剂和粘度指数改进剂。指定的抗氧化剂是二硫代磷酸锌,泡沫抑制剂是硅油。ALSO:通过形成包含油溶性分散剂,非挥发性,油溶性稀释液的混合物来生产含碳酸钡的分散体,碱值至少为110的上述氧化钡和/或氢氧化物溶液的乙二醇醚溶液,以及具有式ROCH2.CH2.OH或R1.O.CH2.CH2.O.CH2.CH2的醚.OH,其中R是包含1-6个碳原子的烃基,R1是包含1-4个碳原子的烃基,并且使CO2通过混合物以生成所需的分散材料,并在碳化之前或之后除去不希望的挥发性材料通过蒸汽处理或沸腾进行分离以产生所需的分散体。优选的分散剂是油溶性磺酸,羧酸或硫化磷处理的烯烃及其金属盐。油溶性稀释液优选是矿物或合成润滑油。对于其中存在的每摩尔中和的含钡碱,可以使1-5摩尔的CO 2通过混合物。给出了反应混合物的优选组成,并且优选的醚是2-甲氧基-乙醇。混合可以在大气压下在25-120℃的温度下进行,并且CO 2可以在21-63℃的温度下鼓泡通过混合物,直到其对对萘酚苯并指示剂呈酸性。 :溶液包含具有式ROCH 2 OH或R 10 CH 2 CH 2的二醇醚。 O.CH2.CH2.OH,其中R为含1至6个碳原子的烃基,R1为含1-4个碳原子的烃基,醚在溶液中具有按碳酸根计算的按重量计至少18.5%的Ba。可以通过优选以小增量将氧化钡和/或氢氧化钡添加到二醇醚中来制备溶液,以避免由于发生放热反应而导致混合物的过度加热。该添加也优选地在惰性气体(例如氮气)的覆盖下进行。 N2在少量氧化抑制成分的存在下二叔丁基甲酚的含量为0.025至0.1%(重量)。如果需要一次添加整个钡碱,则必须将混合物冷却以保持温度低于b.pt。乙二醇在消除反应后,将混合物加热至80℃至沸点之间的温度。将乙二醇倒入10-30分钟,然后冷却。在实施例中,使用的醚是2-甲氧基乙醇。

著录项

  • 公开/公告号CH490479A

    专利类型

  • 公开/公告日1970-05-15

    原文格式PDF

  • 申请/专利权人 CONTINENTAL OIL COMPANY;

    申请/专利号CH19650006338

  • 发明设计人 RICHARD BRADLEYWILLIAM;C. SIASROY;

    申请日1965-05-06

  • 分类号C10M1/10;

  • 国家 CH

  • 入库时间 2022-08-23 11:20:36

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