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- W4362466464 abstract "The aim of this research paper is to develop a chemical kinetic model, based on the mechanism of surface reactions, for air–steam gasification of eucalyptus wood sawdust (CH1.63O1.02) and analyze the hydrogen-rich syngas production. Experiments are performed on a bubbling fluidized-bed gasifier using air–steam as a gasifying agent. For validation of the developed kinetic model, the outcome of the model is compared with that of experimental data, which shows a root-mean-square error of less than 4. Different parameters such as equivalence ratios (0 ≤ ER ≤ 0.4), particle size (100 ≤ Dp ≤ 1000 μm), gasification temperature (900 ≤ T ≤ 1200 K), pressure (1 ≤ P ≤ 20 atm), and steam-to-biomass ratio (0 ≤ SBR ≤ 2) are considered for the analysis. The one-parameter-at-a-time concept is employed to maximize the production of H2-rich syngas. Results indicate that the maximum concentration of hydrogen is 55.04 vol % (experimental) and 51.81 vol % (predicted) at optimum conditions: ER = 0, Dp = 100 μm, T = 1100 K, P = 1 atm, and SBR = 0.75. Gasification performance parameters such as hydrogen gas yield, heating values, cold gas efficiency, etc., are evaluated." @default.
- W4362466464 created "2023-04-05" @default.
- W4362466464 creator A5039702965 @default.
- W4362466464 creator A5050198084 @default.
- W4362466464 date "2023-03-31" @default.
- W4362466464 modified "2023-09-25" @default.
- W4362466464 title "Chemical Kinetic Modeling of Air–Steam Gasification of Eucalyptus Wood Sawdust for H<sub>2</sub>-Rich Syngas Production" @default.
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- W4362466464 doi "https://doi.org/10.1021/acsomega.3c00908" @default.
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