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• W2316451421 endingPage "1991" @default.
• W2316451421 startingPage "1982" @default.
• W2316451421 abstract "Photocatalytic technology has received increasing attention owing to its various advantages. In this work, we designed a fluidized-bed photocatalytic reactor using H2S simultaneously as the bubbling gas for catalyst suspension and as the feed for hydrogen production. The photocatalyst distribution was simulated by CFD with a Eulerian model. The simulation results indicated that the fluidizing time showed a linear relationship with the inlet gas velocity and that the optimal inlet gas velocity was between 30 and 50 mL/min. Further, light energy absorption characteristics, in both homogeneous and heterogeneous media, were simulated by the Monte Carlo method. Our study showed that light energy absorption is affected by the nonuniform distribution of the catalyst particles and that finding the optimum optical thickness in chemical reaction space and the optimal height for catalyst fluidization is essential for reactor design. The simulation results and the related predictions are helpful for the design and optimization of fluidized-bed photocatalytic reactors." @default.
• W2316451421 created "2016-06-24" @default.
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• W2316451421 date "2013-01-23" @default.
• W2316451421 modified "2023-09-22" @default.
• W2316451421 title "Photocatalytic Hydrogen Production from Refinery Gas over a Fluidized-Bed Reactor I: Numerical Simulation" @default.
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• W2316451421 doi "https://doi.org/10.1021/ie3023127" @default.
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