Published October 2021 | Version v1
Journal article

Application of Zn-ferrite towards thermochemical utilization of carbon dioxide: A thermodynamic investigation

  • 1. Department of Chemical Engineering, College of Engineering, Qatar University, P. O. Box – 2713, Doha (Qatar)
  • 2. Department of Chemical and Biological Engineering, South Dakota School of Mines and Technology, Rapid City, South Dakota 57701-3995 (United States)
  • 3. Department of Chemical and Life Science Engineering, Virginia Commonwealth University, Richmond, VA 23284 (United States)

Description

Highlights: • Zn-ferrite-based CDS cycle in thermodynamically studied for the first time. • The energy demand of the heating of inert sweep gas and separation of gases is considered. • The solar energy required to drive the cycle increases due to the rise in the inert sweep gas flowrate. • The energy required for the heating of ZnFe2O4, inert sweep gas, and CO2 plays a vital role. • Maximum ηsolar-to-fuel is attained when gas-to-gas heat recovery effectiveness was held at 0.9. This study reports a thermodynamic analysis of ZnFe2O4 based CO2 splitting cycle. The model developed is evaluated by using HSC Chemistry software. Effects of the influence of the ratio of the molar flow rate of inert sweep gas to the molar flow rate of ZnFe2O4, thermal reduction temperature, and gas-to-gas heat recovery effectiveness on thermal energy required to drive the cycle and the solar-to-fuel energy conversion efficiency are investigated at reduction nonstoichiometry of 0.1. The decrease in the reduction temperature is significant when the ratio of the molar flow rate of inert sweep gas to the molar flow rate of ZnFe2O4 increases from 10 to 30. At a steady gas-to-gas heat recovery effectiveness equal to 0.7, a rise in the ratio of the molar flow rate of inert sweep gas to the molar flow rate of ZnFe2O4 from 10 to 90 is responsible for an increase in the thermal energy required to drive the cycle above 184.9 kW by a factor of 1.45 and decrease in the solar-to-fuel energy conversion efficiency by 4%. At gas-to-gas heat recovery effectiveness equal to 0, the difference between the thermal energy required to drive the cycle at the ratio of the molar flow rate of inert sweep gas to the molar flow rate of ZnFe2O4 equal to 10 and 100 is 346.5 kW. However, as the gas-to-gas heat recovery effectiveness increases to 0.9, this difference decreases to 11.8 kW. Because of this, the reduction in the solar-to-fuel energy conversion efficiency also drops to 0.6%. Therefore, a maximum possible solar-to-fuel energy conversion efficiency equal to 16.8% can be achieved.

Availability note (English)

Available from http://dx.doi.org/10.1016/j.enconman.2021.114528

Additional details

Identifiers

DOI
10.1016/j.enconman.2021.114528;
PII
S0196890421007044;

Publishing Information

Journal Title
Energy Conversion and Management
Journal Volume
245
Journal Page Range
vp.
ISSN
0196-8904
CODEN
ECMADL

Optional Information

Copyright
Copyright (c) 2021 The Author(s). Published by Elsevier Ltd.