Method for producing high-grade lubricant base oil through hydrogenating of hydrocracking tail oil
A technology for hydrocracking tail oil and lubricating base oil, which is applied in the fields of hydrotreating process, petroleum industry, and hydrocarbon oil treatment. It can solve the problems of low base oil yield, achieve high activity, increase selectivity, and improve The effect of low temperature fluidity
Patent Information
- Authority / Receiving Office
- CN · China
- Patent Type
- Applications(China)
- Current Assignee / Owner
- Publication Date
- 2013-09-18
Smart Images
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Abstract
Description
technical field
[0001] The invention belongs to the field of petrochemical industry, and in particular relates to a method and equipment for producing high-grade lubricating oil base oil through hydrogenation of hydrocracking tail oil. Background technique
[0002] The content of lubricating oil base oil in finished lubricating oil is usually 70% to 99%. The quality of base oil directly affects the quality of lubricating oil. The most important thing in China's lubricating oil market is internal combustion engine oil, which is divided into high, medium and low grades in terms of quality, and their market shares are 10%, 30% and 60% respectively. The current production situation of lubricating oil in my country is that the output of low-grade products is too large, the proportion of medium and high-end products is relatively small, and the gap of high-end products is relatively large. Moreover, there is a big gap between the quality and the international level. The main reas...
Examples
Embodiment 1
[0038] First, the hydrocracking tail oil (see Table 2 for properties) enters the vacuum pre-fractionator for vacuum fractionation. The cut point of vacuum fractionation is 430°C, and the light fraction of hydrocracking tail oil with an end boiling point ≤ 430°C is taken as No. 4 As the base oil, the heavy fraction of hydrocracking tail oil with an initial boiling point > 430°C was used as the No. 6 base oil (see Table 2 for properties). The base oil is mixed with new hydrogen and the circulating hydrogen boosted by the circulating hydrogen compressor, and then enters the isomerization dewaxing and supplementary refining reactor in turn (see Table 3 for the catalyst used); the reaction is separated from the gas and liquid, and the gas is desulfurized and then compressed The machine pressurization is mixed with fresh hydrogen as the raw material of the isomerization dewaxing-supplementary refining reactor, and the liquid product is often distilled under reduced pressure to obtain...
Embodiment 2
[0040] The raw material that adopts, technological process and corresponding catalyzer are identical with embodiment 1, and what differ with embodiment 1 is the technological condition selected, and reaction technological condition is shown in Table 4, and the result and the property of the lubricating base oil product of generation are shown in Table 5 and Table 7. Comparative example 1