TECHNOLOGY FOCUS - INORGANIC CHEMISTRY - Preferred Components: The nonsulfided hydrotreating catalyst comprises at least one metal comprising groups 6, 8, 9, and 10 of the periodic table. The hydrotreating catalyst comprises molybdenum, where the first product, a proportion of at least one of paraffins resulting from cracking processes or iso-paraffins is greater as compared to a corresponding proportion of at least one of paraffins resulting from cracking processes or iso-paraffins obtained when the hydrotreating catalyst has less or no molybdenum. The hydrotreating catalyst comprises nickel, where the first product, a proportion of hydrocarbons having an odd number of carbon atoms is greater as compared to a proportion of hydrocarbons having an odd number of carbon atoms when the hydrotreating catalyst has less or no nickel. The hydrotreating catalyst comprises at least one metal comprising palladium, platinum and/or nickel. The hydrotreating catalyst comprises nickel and molybdenum or cobalt and molybdenum. The hydrotreating catalyst further comprises a support comprising alumina and/or silica.    TECHNOLOGY FOCUS - ORGANIC CHEMISTRY - Preferred Method: The method further comprises: controlling the average temperature during hydrotreating to be a higher average temperature, such that in the first product the ratio of hydrocarbons having an odd-number of carbon atoms to hydrocarbons having an even-number of carbon atoms is higher, or the ratio of cyclic hydrocarbons to hydrocarbons having an even-number of carbon atoms is higher, as compared to a corresponding ratio obtained where the average temperature used during hydrotreating is controlled to be a lower average temperature; and controlling the average temperature during hydrotreating to be a lower average temperature, such that in the first product the ratio of hydrocarbons having an odd-number of carbon atoms to hydrocarbons having an even-number of carbon atoms is lower, or the ratio of cyclic hydrocarbons to hydrocarbons having an even-number of carbon atoms is lower, as compared to a corresponding ratio obtained, where the average temperature used during hydrotreating is controlled to be a higher average temperature. The hydrotreating is performed at 340-400 degrees C or 470-530 degrees C and a pressure of 500-750 psig or 750-1000 psig. The method further comprises: subjecting the first product to at least one process of isomerization, cracking, and aromatization to produce a second product for use as gasoline, naphtha, kerosene, jet fuels, or diesel fuels. Preferred Components: In the method, greater than 90 mol.% of the fatty acid groups in the renewable TAG, renewable FFA, and renewable 1-5C FAE have an even number of carbon atoms. The TAG in the feedstock is derived from at least one of plants, animals, algae and/or other microorganisms. The renewable fatty acid in the feedstock is derived from hydrolysis of a renewable TAG. The renewable 1-5C FAE in the feedstock is derived from a renewable TAG. The first product comprises greater than 50 wt.% of saturated and aromatic hydrocarbons. EXAMPLE - Coconut oil was supplied to reactor at a rate of 1 pound/hour. Hydrogen was supplied at a rate of 20 standard cubic feet per hour (scfh). The reactor was maintained at 340 degrees C. The hydrogen pressure was regulated to 80 psi. The temperature and flow conditions were maintained for 3 hours once steady-state conditions were achieved. The product was collected and analyzed.