Abstract.In this paper, we present a superstructure optimization approach for the integration of the simultaneous production of liquid fuels and hydrogen from switchgrass and shale gas. The process is based on FischerTropsch technology in which the shale gas is reformed with steam, while the switchgrass is gasified and reformed (with steam or partial oxidation). The raw gas is cleaned up, including removal of the sour gases, and its composition is adjusted (using either water gas shift reaction or pressure swift adsoprtion) and the liquid fuels are obtained in an FT reactor. The heavy liquids are upgraded using hydrocracking to increase the yield towards FTdiesel. A sensitivity study on the raw material prices reveals that production costs for the biomass-shale gas facility are below $1/gal as long as biomass price is below $100/t and the price of the shale gas is not higher than $11.5 /MMBTU. Furthermore, hydrogen is produced as long as the demand for liquid fuels is met and there is enough shale gas available.