Fanxing Li1, Deepak Sridhar2, Hyung Rae Kim2, Liang Zeng2, Fei Wang2, and L. -S. Fan2. (1) The Ohio State University, 140 W 19th Ave, Columbus, OH 43210, (2) Chemical and Biomolecular Engineering, The Ohio State University, 140 West 19th Avenue, Columbus, OH 43210
The Syngas Chemical Looping (SCL) process converts gaseous fuels such as syngas and hydrocarbons into hydrogen while capturing 100% of the CO
2 generated. The SCL process simplifies the overall fuel conversion scheme while reducing pollutants in an indirect but highly effective manner. This is achieved via a specially tailored Fe
2O
3 based composite particle. As a result, hydrogen production cost is substantially reduced. Extensive demonstrations of the SCL process have been carried out under a bench scale (2.5 KWt) unit using coal-derived syngas, natural gas, and other light hydrocarbons as feedstock. Hydrogen with an average purity higher than 99.95% was produced.
In this paper, the SCL process demonstrations are discussed. ASPENŽ simulation based on the bench scale demonstration results was used to analyze the SCL process. Process economics for the SCL process is also presented.