Production of high quality lubricant bright stock

Abstract

A process for producing a lubricant bright stock from a very heavy feed obtained from a petroleum crude is disclosed. The bright stock produced by the present process has a reduced cloud point and better oxidation stability relative to bright stocks prepared by conventional methods. The process comprises the steps of providing a petroleum residuum-derived stream; separating the residuum-derived stream at a distillation cut point in the range of 1150° F. to 1300° F., into a heavy fraction and at least one light fraction; hydrocracking the at least one light fraction under conditions to reduce the concentration of sulfur and nitrogen to suitable levels for hydroisomerization dewaxing; and dewaxing at least a portion of the hydrocracked stream under hydroisomerization conditions to produce a lubricant bright stock.

Description

FIELD OF THE INVENTION [0001] The present invention relates to a process for producing a high quality lubricant bright stock from heavy petroleum feedstocks. BACKGROUND OF THE INVENTION [0002] This invention is directed to a process for preparing a high quality lubricant bright stock from heavy petroleum feedstocks. These heavy feedstocks are often contaminated with sulfur, nitrogen, asphaltenic and metal contaminants, which must be removed in preparing the lubricant base stock. They also generally contain significant amounts of waxy materials. [0003] Low valued oils such as deasphalted oil (DAO) are increasingly being hydrotreated and used as FCC cracker feed to produce gasoline. Severity of deasphalting is much less for making fuels than for making lubricant bright stock. Consequently, the purity of fuels-application DAO is too low to make lubricant bright stock with adequate stability for use in finished lubricant applications. However, increasingly stringent mandated limits on g...

AI Technical Summary

Benefits of technology

[0007] The present invention relates to a process for producing a lubricant bright stock from a very heavy feed, having a normal boiling end point within the range of 1150° F. to 1300° F. The very heavy feed is obtained from petroleum crude. The bright stock produced by the present process has a reduced cloud point and better oxidation stability relative to bright stocks prepared by conventional methods.

Problems solved by technology

Conventional methods for preparing bright stock by hydroisomerization dewaxing a vacuum residuum fraction, a hydrocracked vacuum residuum fraction, deasphalted oil or hydrocracked deasphalted oil generally produces a bright stock with unacceptable haze-forming tendencies.