Patent application number | Description | Published |
20080287717 | Feedstock preparation of olefins for oligomerization to produce fuels - A feedstock containing at least 1 wt % butenes, at least 1 wt % pentenes, at least 1 wt % hexenes, at least 10 wppm C | 11-20-2008 |
20090216048 | Process for producing phenol and methyl ethyl ketone - In a process for producing phenol and methyl ethyl ketone, benzene and a C | 08-27-2009 |
20120006722 | Integrated Vacuum Resid To Chemicals Conversion Process - A process and apparatus for cracking a hydrocarbon feed containing resid, comprising: heating a hydrocarbon feedstock containing resid; passing said heated hydrocarbon feedstock to a vapor/liquid separator; flashing said heated hydrocarbon feedstock in said vapor/liquid separator to form a vapor phase and a liquid phase containing said resid; passing at least a portion of said resid-containing liquid phase from said vapor/liquid separator to a thermal conversion reactor operating at 649° C. or more, wherein the thermal conversion reactor contains coke particles; and converting at least a portion of said resid into olefins. | 01-12-2012 |
20120184442 | Ultra Pure Fluids - The invention relates to hydrocarbon fluids having high purity with respect to at least one of sulfur species, nitrogen species, oxygenated species, and unsaturated species, particularly hydrocarbon fluids low in aromatics, a method of making said hydrocarbon fluids, a catalyst for use in said method, an apparatus whereby said method may be practiced, and uses of said fluids. | 07-19-2012 |
20130115143 | Integrated Vacuum Resid To Chemicals Conversion Process - A process and apparatus for cracking a hydrocarbon feed containing resid, comprising: heating a hydrocarbon feedstock containing resid; passing said heated hydrocarbon feedstock to a vapor/liquid separator; flashing said heated hydrocarbon feedstock in said vapor/liquid separator to form a vapor phase and a liquid phase containing said resid; passing at least a portion of said resid-containing liquid phase from said vapor/liquid separator to a thermal conversion reactor operating at 649° C. or more, wherein the thermal conversion reactor contains coke particles; and converting at least a portion of said resid into olefins. | 05-09-2013 |
20130296623 | Process for the Production of Xylenes and Light Olefins - In a hydrocarbon upgrading process, a hydrocarbon feed is treated in at least one of a steam cracker, catalytic cracker, coker, hydrocracker, and reformer under suitable conditions to produce a first stream comprising olefinic and aromatic hydrocarbons. A second stream composed mainly of C | 11-07-2013 |
20150158785 | Production of C2+ Olefins - Carbon monoxide and molecular hydrogen are converted to an alcohol mixture, which is separated into a first, methanol-containing stream and a second, C | 06-11-2015 |
20150274609 | Production of Aromatics and C2+ Olefins - The invention relates to converting a mixture of carbon monoxide and molecular hydrogen to an alcohol mixture, which is separated into a first, methanol-containing stream and a second, C | 10-01-2015 |