2025 AIChE Annual Meeting

(318d) Optimizing Tar Cracking in Sorption-Enhanced Gasification: Decomposition of Naphthalene Using Dolomite Catalysts.

Authors

Rashmi Charde - Presenter, University of Utah
Kevin Whitty, The University of Utah
Michael Nigra, University of Utah
Sorption-enhanced gasification (SEG) of biomass is a promising technology that produces hydrogen-rich syngas. Using bed materials with high CO2 sorption capacity shifts the equilibrium of water gas shift reaction towards producing more H2. Tar production is considered the Achilles heel of biomass gasification. While most tar cracking studies focus on high temperatures and fixed bed reactors, SEG is operated with a fluidized bed and at lower temperatures due to limestone and dolomite's carbonation/calcination equilibrium. This study investigates the decomposition of naphthalene, a model tar compound, at 700oC in a fluidized bed reactor. In an inert atmosphere, calcined dolomite showed 96% conversion of naphthalene. This conversion deteriorated to 33% after 4 hours of operation. Thermogravimetric analysis performed for the spent catalyst revealed mass loss above 600oC in an air atmosphere, indicating carbon accumulation on the catalyst. The absence of oxidizing agents like CO2 and steam exacerbated the catalyst deactivation. Introducing 10 volume % CO2 into the reactor gave significant insight into dry reforming of naphthalene. Naphthalene conversion remained consistent over 8 hours of reaction time at an average of 28%. The catalyst weight increased from 30g to 43 g after the experiment because the CaO/CaCO3 equilibrium was in the carbonation zone. The CO2 adsorbed on the surface of CaO, thus reducing the amount of catalytic sites available for the naphthalene. Temperatures of 800 and 900oC resulted in 91% and 100% conversion, respectively, by shifting the CaO/CaCO3 equilibrium in the calcination zone. However, achieving efficient conversions at SEG operating parameters remains challenging. To enhance catalytic performance at 700oC, we propose a bimetallic Ni-Fe/dolomite doped in K2O catalyst that is synthesized via a sequential co-impregnation method. The presence of nickel would improve the tar-cracking abilities. The combination of dolomite’s CO2 sorption capacity and Fe catalyzing the WGS reaction would significantly enhance hydrogen production.