Cody J. Wrasman, Brittney E. Petel, Carson Pierce, Kellene A. Orton, Scott E. Palmer, Jacklyn N. Hall, Hacksung Kim, Fulya Doğan, Theodore R. Krause, Huamin Wang, Xinbin Yu, Stefano Dell’Orco, Kinga A. Unocic, Alexandre C. Foucher, Tomas Grejtak, David A. Cullen, Grace Blaskowski, Frederick G. Baddour, Xiaolin Chen, Kristiina Iisa, Abhijit Dutta, Susan E. Habas, Michael B. Griffin
Catalytic fast pyrolysis (CFP) is a promising strategy for producing hydrocarbon transportation fuels from biomass feedstocks. However, catalyst development is needed to increase bio-oil yields and enhance process economics. In this work, we demonstrate how post synthetic modification of formed ZSM-5 with phosphorus shifts CFP selectivity from coke and light gases toward the desired bio-oil product. Microscale experiments demonstrated reduced coke production relative to unmodified ZSM-5 and identified an optimal P loading. Extensive catalyst characterization revealed that P interacted with Al sites to reduce the acid site density, with preferential binding to the strongest acid sites. Insights from the microscale experiments were leveraged to produce kilogram quantities of formed P-ZSM-5 for evaluation in a larger semi-integrated process. These experiments generated liters of bio-oil that was hydrotreated and fractionated into gasoline, diesel, and jet cuts. The phosphorus-modified ZSM-5 improved CFP bio-oil yield, resulting in an 11% relative increase in the carbon yield from biomass to aviation fuel and a 14% decrease in the minimum fuel selling price. These results highlight the impact targeted changes in catalyst acidity, achieved by adding 2.5 wt % P, can have on the carbon efficiency and feasibility of fuel production from biomass feedstocks.