The higher the temperature (range 200 °-300 ° C) on every type of catalyst, the value of the total yield of the resulting product will be more and more. This is in accordance with the research done Hong et al. (2014) that as the increase of the temperature of 200 ° C to 300 ° C, the product yield of deoxygenation p phenol. The increase in temperature in General would increase the activity of deoxygenation for every type of catalyst, which is characterized by conversion into products anisol is high. In addition, the rise in temperature causes the teraktifkan reactants to the catalyst will be more and more so the catalytic reaction is increased. An increase in the yield of the product total catalyst CoMo/USY, Co-Mo/USY, Mo-Co/USY is comparable with USY. The relationship type catalyst with total yield (%) with temperature variations anisol reaction time for 1 hour is presented in Figure 4.1.
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