Raffinate hydroconversion for production of high performance base stocks
AssigneeExxonMobil Technology and Engineering Company
InventorsJason T. Calla, Will G. Fisher, Jr., Eric D. Joseck, Seth D. Fortney
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AssigneeExxonMobil Technology and Engineering Company
InventorsJason T. Calla, Will G. Fisher, Jr., Eric D. Joseck, Seth D. Fortney
Estimating the term…
Systems and methods are provided for production of base stocks with a viscosity index of at least 120 and/or a sulfur content of 300 wppm or less and/or a kinematic viscosity at 100° C. of 3.0 cSt to 8.0 cSt by hydroconversion of a raffinate from aromatic extraction of a feed. The base stocks can further have a reduced content of 3+ ring naphthenes, such as 4.0 wt % or less, or 1.0 wt % or less. The base stocks can be produced by performing an elevated amount of feed conversion relative to 370° C. during hydroconversion of the raffinate, and optionally additional conversion during catalytic dewaxing of the hydroconverted raffinate. The base stocks can optionally be blended with additional base stocks and/or lubricant additives for production of lubricant compositions.
A base stock comprising a viscosity index (VI) of 130 to 140, a sulfur content of 50 wppm or less, a saturates content of at least 90 wt %, a Noack volatility of 14 wt % or less, a pour point of −15° C. or less, a kinematic viscosity at 40° C. of greater than 20 cSt to 40 cSt, and a kinematic viscosity at 100° C. of 3.5 to 4.5 cSt, the base stock further comprising a 3+ ring naphthene content of 0.5 wt % or less.
A base stock comprising a viscosity index (VI) of 135 to 140, a sulfur content of 50 wppm or less, a saturates content of at least 90 wt %, a Noack volatility of 14 wt % or less, a pour point of −15° C. or less, a kinematic viscosity at 40° C. of greater than 20 cSt to 40 cSt, and a kinematic viscosity at 100° C. of 3.5 to 4.5 cSt, the base stock further comprising a 3+ ring naphthene content of 1.0 wt % or less.
A base stock comprising a viscosity index (VI) of 125 to 140, a sulfur content of 50 wppm or less, a saturates content of at least 90 wt %, a Noack volatility of 5 wt % or less, a pour point of −15° C. or less, and a kinematic viscosity at 100° C. of 4.5 to 8.0 cSt, a kinematic viscosity at 40° C. of greater than 20 cSt to 40 cSt, the lubricant base stock further comprising a 3+ ring naphthene content of 4.0 wt % or less.
A lubricant composition comprising:
Dependencies are inferred from the claim text.