Suppose that you are investigating a coal/biomass-to-liquids (CBTL) process involving Fischer-Tropsch (FT) synthesis from syngas. Syngas flows over a temperaturesensitive cobalt catalyst to produce FT hydrocarbons as described in Equation 1: CO + 2 H2 -CH2- + H2O Hrxn = -165 kJ/mol (1) where -CH2- represents a single link in a carbon chain. Assume a process goal is to maximize yields exiting the reactor without using a recycle stream. Hypothesize the results of using a fluidized bed reactor and packed bed reactor for the application.