TECHNOLOGY FOCUS - INORGANIC CHEMISTRY - Preferred Components: The catalyst is a metal catalyst, an organometallic catalyst, a nanosphere catalyst, a supported catalyst, or a soluble catalyst (preferably organomolybdenum compound). In the process (P3), the catalyst is an alkali metal.    TECHNOLOGY FOCUS - ORGANIC CHEMISTRY - Preferred Process: The process (P1) of generating free radicals is not preceded by a process for disassociating the light gases. The reactor is a non-thermal plasma reactor (preferably gliding arc reactor, a micro-plasma generator, or a homogenizer). The free radicals are generated by high shear, ultrasonic, cavitation and/or high energy mixing devices. The process (P1) further involves adding a catalyst in the reactor. The process (P1) forms fatty acid ethyl esters (FAEE) and glycerol as byproducts, where the glycerol byproduct is further reacted to form at least one glycerol ether product, which is added to the hybrid fuel. In the process (P2), the step of reforming the light gases is preformed at a pressure of less than 5 atm; the process is conducted at 200-500 degrees C; and the reforming step is at least one of dry reforming, steam reforming, partial oxidation, and formation of methyl radicals. In the process (P3), the reacting step is performed under elevated temperature and/or pressure. Preferred Components: The first reactant further comprises a second liquid fuel feed. The second fuel product is a hybrid fuel produced from the process. In the process (P3), the carbonaceous feedstock is coal, biomass and/or petroleum coke. The first fuel product further includes glycerol ether. Preferred Fuel: The hybrid fuel comprises the first fuel product (20 wt.%) and the second fuel product (80 wt.%); water (up to 20%); polynuclear aromatic compounds ( not greater than 5%); aromatics ( not greater than 20%). The pour point of the hybrid fuel is -25 to -35 degrees C; or 15 degrees F lower than the pour point of the second fuel product in isolation. Preferred Apparatus: The exit zone is interposed between and in fluid communication with the path defined by the electrodes and the second inlet. The apparatus further comprises Helmholtz coils located in the exit zone; a catalyst located in the exit zone; heating coils capable of heating the contents of the apparatus to a specified temperature; a low work force cathode, thus increasing electron flow and/or electron density, where the low work force cathode includes thorium. EXAMPLE - No suitable example given.