(514h) Solar Fuel Production Via Germanium Oxide-Based Thermochemical Conversion of CO2 | AIChE

(514h) Solar Fuel Production Via Germanium Oxide-Based Thermochemical Conversion of CO2

Authors 

Bhosale, R. - Presenter, South Dakota School of Mines and Technology
Adams, S., University of Tennessee
Allen, Z., University of Tennessee
Bennett, G., University of Tennessee
Berezniovas, E., University of Tennessee
Bishop, T., University of Tennessee
Bonnema, M., University of Tennessee
Clutter, S., University of Tennessee
Fagan, R., University of Tennessee
Halabrin, J., University of Tennessee
Hobbs, M., University of Tennessee
Hunt, D., University of Tennessee
Ivarra, M., University of Tennessee
Jordan, M., University of Tennessee
Karunanithi, P., University of Tennessee
Mcreynolds, J., University of Tennessee
Ring, V., University of Tennessee
Smith, S., University of Tennessee
West, J., University of Tennessee
Solar fuels such as solar H2 or syngas are considered to have the potential to fulfill the energy demand of the future. Thermochemical conversion of H2O and/or CO2 for producing solar fuels is one of the available possible technologies. Several metal oxides, which include zinc oxide, tin oxide, ceria, doped ceria materials, iron oxide, doped iron oxide materials (ferrites), and perovskites, have been investigated. One of the major issues with utilizing all these mentioned oxides is the requirement for a higher reduction temperature. We are currently working on a two-step germanium oxide redox cycle to overcome this issue. The germanium oxide-based redox cycle is thermodynamically investigated in this investigation to estimate the maximum possible theoretical solar-to-fuel energy conversion efficiency. After understanding the equilibrium compositions associated with the cycle, a detailed process flow configuration is developed. The process flow configuration includes reduction and oxidation reactors, heat exchangers, auxiliary heaters and coolers, an ideal fuel cell, gas separation units, recycle streams, etc. A thermodynamic model is developed, and its computations are carried out using the data obtained from the commercially available HSC Chemistry software. The computational thermodynamic modeling is carried out by varying the thermal reduction temperatures and inert gas flow rates, neglecting the solid-to-solid heat recovery and varying the gas-to-gas heat recovery effectiveness, and including separation units and surface losses from the reduction reactor. Overall, the influence of all the above variables on the solar energy input required to drive the cycle and solar-to-fuel energy conversion efficiency is studied in detail, and the obtained results will be presented.

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