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The partial oxidation of propane to acrolein is studied in a dual bed membrane reactor.
Furthermore, we compared the performance between single and dual bed reactors.
Especially, the catalyst stability in the gasification of rice straw clearly was enhanced by using the fluidized dual bed reactor.
A dual bed reactor concept was chosen to productively couple two different chemistries to direct reaction towards specific products.
Application of the testing methodology for process study including regeneration protocol and dual bed adsorbent ratio of an industrial adsorption chamber has been demonstrated.
We propose a hybrid HI decomposer, which combines a high-temperature catalytic decomposition reactor with a dual bed temperature-swing decomposer.
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Variations in the C2H4/C2H6 ratio have been studied as a function of the mass of catalyst, the reactor dimensions, and for different arrangements of catalysts in dual beds.
We have further measured the stability of the Na Fe3O4/HZSM-5 catalyst with dual-bed configuration (Fig. 4c).
A novel dual-bed system was designed to produce hydrogen through photocatalytic water splitting.
The selectivity to aromatic hydrocarbons over composite catalysts is higher than that in dual-bed.
(c) The stability of the Na Fe3O4/HZSM-5 catalyst with dual-bed configuration under the same reaction conditions as Fig. 1a.
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