Thermodynamic analysis of hydrogen production by steam and autothermal reforming of soybean waste frying oil

Hydrogen production via steam and autothermal reforming of soybean waste frying oils (WFOs) is thermodynamically investigated via the Gibbs free energy minimization method. The thermodynamic optimum conditions are determined to maximize hydrogen production while minimizing the methane and carbon monoxide contents and coke formation. Equilibrium calculations are performed at atmospheric pressure over a wide range of temperatures (400–1200 °C), steam-to-WFO ratios (S/C: 1–15) and oxygen-to-WFO ratios (O/C: 0.0–2.0). The baseline case used for the study considers soybean WFO after 8 h of use (WFO8). The influence of frying time on the performance of reforming reactors is also discussed. sults show that the optimum conditions for steam reforming can be achieved at reforming temperatures between 650 °C and 850 °C and at a steam to carbon molar (S/C) ratio of approximately 5. The recommended operation conditions for the SR of WFO8 are proposed to be T = 650 °C and S/C ratio = 5. Under these conditions, a hydrogen yield of 169.83 mol/kg WFO8 can be obtained with a CO concentration in the SG of 3.91% and trace CH4 (0.03%), without the risk of coke formation. en production from autothermal systems can be optimized at temperatures of 600–800 °C, S/C ratios of 3–5, and O/C ratios of 0.0–0.5. Under these conditions, thermoneutrality is obtained with O/C ratios of 0.391–0.455. The recommended thermoneutral conditions are S/C = 5, T = 600 °C and O/C = 0.453. Under these conditions, 146.45 mol H2/kg WFO8 can be produced with only 2.89% CO and 0.06% CH4 in the synthesis gas. fect of frying time of soybean WFO on hydrogen productivity is shown to be negligible.