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manufacturing method of lubricating oil and viscosity index (index of the Production viscosity Iubricants)

机译:润滑油的制造方法和粘度指数(生产粘度指标的指数)

摘要

low oil content of the petroleum wax supply of raw materials can be decomposed in the two - stage - to the isomerization method and viscosity index lubricating oil into the way, just as in the supply of materials, and the conditions of the first decomposition stage can be a general the 30 or 40 weight% of the supply of the lubricating oil of the raw material into the resultant. the first step is to open the 800 psig (5617 PkPaa) above the supply of raw material in hydrogen pressure in the presence of the aromatic components is amorphous catalyst under the presence of the organism. the second step is to take the first step of the resultant from the second stage to direct investment or low voltage, representative of psig (200 or 1000 or 6996 1480 PkPaa) can perform.the second stage also welcomed to precious metal containing zeolite beta catalyst. the second stage is relatively low temperature of 600 degrees f to be 650 (316 or 343 degrees) in the temperature of operation. the floating point to the dewaxing stage can be used.
机译:含油量低的石油蜡原料可以在两阶段分解—以异构化方法和粘度指数法转化成润滑油的方式,就像在原料供应中一样,并且可以在第一分解条件下进行通常为原料中润滑油的30或40重量%。第一步是在有机物存在下,在芳香族成分为无定形催化剂的情况下,在氢气压力下,在原料压力上方打开高于800 psig(5617 PkPaa)的原料。第二步是将第一步的产物从第二步转移到直接投资或低压,可以代表psig(200或1000或6996 1480 PkPaa)。第二步也欢迎使用含贵金属的β沸石催化剂。第二阶段是工作温度为600华氏度的相对较低的温度,达到650度(316或343度)。可以使用脱蜡阶段的浮点数。

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