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PREPARATION OF TRANSFORMER OIL COMPOSITION FROM RAW FOR HYDROCRACKING OIL
PREPARATION OF TRANSFORMER OIL COMPOSITION FROM RAW FOR HYDROCRACKING OIL
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机译:用原料制备用于加氢裂化油的变压器油组合物
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摘要
PURPOSE: To provide a formulated transformer oil having properties equivalent to those of a formulated naphthenic transformer oil by fractionating a hydrocracked paraffinic petroleum hydrocarbon stock, dewaxing the resultant distillate with a solvent, and adding to the dewaxed distillate an antioxidant and/or a pour point depressant. ;CONSTITUTION: A paraffinic petroleum hydrocarbon stock is hydrocracked in the presence of a hydrogenation catalyst at 350°C or lower at a liq. space velocity of 0.2-2.0 V/V/H, a pressure of 35.15-210.9 kg/cm2, a hydrogen purity of 50-100 LV%, a hydrogen treating velocity of 3,000-120,000 SCF/B, and a conversion until 350°C of 50-100. The resultant hydrocracked stock is fractionated to produce a distillate boiling in the transformer oil range (270-350°C), which is cooled to about -24°C and filtered with a dewaxing solvent at -21°C or lower to be dewaxed. To the dewaxed distillate is added 0.005-0.3 wt.% antioxidant and/or 0.01-2.0 wt.% flow point depressant.;COPYRIGHT: (C)1992,JPO
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机译:目的:通过分馏加氢裂化的链烷烃石油原料,用溶剂将所得的馏出液脱蜡,并向脱蜡的馏出物中加入抗氧化剂和/或倾点,来提供具有与配制的环烷基变压器油相同性能的配制的变压器油。抑郁症。 ;组成:链烷烃石油原料在加氢催化剂存在下于350°C或更低的温度下加氢裂化。空速为0.2-2.0 V / V / H,压力为35.15-210.9 kg / cm 2 Sup>,氢气纯度为50-100 LV%,氢气处理速度为3,000-120,000 SCF / B,直到350℃转化为50-100。将所得的加氢裂化的原料分馏以产生在变压器油范围(270-350℃)中沸腾的馏出物,将其冷却至约-24℃并在-21℃或更低的温度下用脱蜡溶剂过滤以脱蜡。向脱蜡的馏出物中加入0.005-0.3wt。%的抗氧化剂和/或0.01-2.0wt。%的流点抑制剂。;版权所有:(C)1992,JPO
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