NOVELTY - Producing fluid hydrocarbon products from solid hydrocarbonaceous material, comprises: providing solid catalyst in a fluidized bed reactor; feeding solid hydrocarbonaceous material to the fluidized bed reactor at mass-normalized space velocity of 0.01-10 hours-1; pyrolyzing within the fluidized bed reactor at least a portion of the hydrocarbonaceous material under reaction conditions to give one or more pyrolysis products; and catalytically reacting at least a portion of the pyrolysis products using the solid catalyst under reaction conditions to give the hydrocarbon products.    USE - The process is useful for producing one or more fluid hydrocarbon products, which comprise aromatic compounds and olefin compounds (claimed), where: the fluid is e.g. a liquid, a supercritical fluid, and/or a gas; and the aromatic compounds are e.g. benzene, toluene, naphthalene and xylene, and olefin compounds are e.g. ethene, propene and butene. The process is useful for the production of biofuel.    ADVANTAGE - The process provides the products with high yields, lower yields of coke formation and/or more controlled product formation (e.g. higher production of the aromatics and/or the olefins relative to other fuels).    DETAILED DESCRIPTION - INDEPENDENT CLAIMS are included for:    (1) a fluid hydrocarbon product comprising a fluid portion of a reaction product of the solid hydrocarbonaceous material, where the fluid hydrocarbon product comprises aromatic compounds (at least 15 wt %) and olefin compounds (at least 7 wt.%) based on total amount of the solid hydrocarbonaceous reactant material used in forming the reaction product and which is calculated as the weight of the aromatic compounds and olefin compounds present in the fluid hydrocarbon product divided by weight of the hydrocarbonaceous material used in forming the reaction product; and    (2) a composition comprising: one or more catalysts, where: at least 95% of the pores of the one or more catalysts have smallest cross-sectional diameters of 5.9-6.3 degrees A or 7-200 degrees A; at least 5% of the pores of the one or more catalysts have smallest cross-sectional diameters of 5.9-6.3 degrees A; and at least 5% of the pores of the one or more zeolite catalysts have smallest cross-sectional diameters of 7-200 degrees A.