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Hydrogenation of dimethyl oxalate (DMO) can be operated in various reactors, such as the packed bed (PB), two‐stage fluidized bed (TSFB), and circulating fluidized bed (CFB) reactors. Fluid dynamic behaviors in these reactors are different and can lead to different transport and reaction behaviors. Recent advances in the computational fluid dynamics (CFD) technique show its great potential in advancing...
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