Fuel compositions from light tight oils and high sulfur fuel oils
Methods are provided to prepare a low sulfur fuel from hydrocarbon sources, such as light tight oil and high sulfur fuel oil, often less desired by conventional refiners, who split crude into a wide range of differing products and may prefer presence of wide ranges (C3 or C5 to C20 or higher) of hydrocarbons. These fuels can be produced by separating feeds into untreated and treated streams, and then recombining them. Such fuels can also be formulated by combinations of light, middle and heavy range constituents in a selected manner as claimed. Not only low in sulfur, the fuels of this invention are also low in nitrogen and essentially metals free. Fuel use applications include on-board large marine transport vessels but also on-shore for large land based combustion gas turbines, boilers, fired heaters and transport vehicles and trains.
1. A formulated fuel comprising light tight oil and hydroconversion effluent boiling at or below highest boiling component of treated soluble deasphalted oil derived from high sulfur fuel oil or other residuals processed by said hydroconversion, said fuel having a range of hydrocarbons from an initial boiling being that of lowest boiling component of light tight oil or lighter materials from said hydroconversion so combined and highest boiling point being that of highest boiling component of said treated soluble deasphalted oil derived from high sulfur fuel oil or other residuals so processed and combined and said fuel having, a density within 820 to 880 Kg/M3 at 15° C., sulfur of 0.5 wt. % or less, and metals of 25 ppmwt or less.
2. A formulated fuel comprising all or a portion of light tight oil and of an effluent of hydroconversion treated by solvent separation to remove heavier asphaltenes and to substantially eliminate metals from unconverted oil of said hydroconversion, said fuel having a range of hydrocarbons from an initial boiling of naphtha to end point of highest boiling oil soluble in propane, butane, pentane, heptane or other paraffinic solvent used in solvent separation preparation of any feed to said hydroconversion, a sulfur of 0.1 wt. % or less, density within 820 to 880 Kg/M3 at 15° C., and metals of 25 ppmwt or less.
3. A formulated fuel of:
(a) all or a portion of a light tight oil and
(b) effluent of residue hydroconversion of
(1) high sulfur fuel oil, either alone with added crude oil or heavy residuals other than high sulfur fuel oil, and
(2) soluble deasphalted oil comprising unconverted oils of hydroconversion of (b)(1) solvent separated to remove insoluble metals and asphaltenes and recycled to said hydroconversion of (b)(1),
said fuel having
(i) sulfur content of 0.1 wt. % or less, density within 820 to 880 Kg/M3 at 15° C., and metals of 25 ppmwt or less,
(ii) initial boiling point being that of lowest boiling component of light tight oil or of said effluent so combined, and
(iii) highest boiling point being that of highest boiling component of light tight oil or of said effluent so combined.