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- W4308486823 abstract "The numerical model of DME reforming hydrogen production reaction system was established and solved by COMSOL software. By analyzing the simulation results of temperature field, flow field and concentration distribution of each component, the reforming effect of spiral heated tube reforming reactor was studied. The effects of Steam-to-Ether, heat flow rate of heating tube, coil number and radius of helical tube to DME conversion, hydrogen yield and catalytic performance of the reactor were investigated by changing reaction conditions and reforming structure. The thermal efficiency of reforming reformer under different working conditions and with different internal structure is obtained by calculation. The results show that 88% DME conversion rate, 86.5% hydrogen production rate and 79.36% thermal efficiency can be obtained in the helical heating tube DME steam reforming reaction system. And the maximum temperature difference of the reaction bed can be controlled within 80 K, about 30% lower than the traditional reactor." @default.
- W4308486823 created "2022-11-12" @default.
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- W4308486823 date "2023-01-01" @default.
- W4308486823 modified "2023-09-27" @default.
- W4308486823 title "Design and optimization of spiral heated tubular dimethyl ether (DME) steam reforming reactor" @default.
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- W4308486823 doi "https://doi.org/10.1016/j.ijhydene.2022.09.295" @default.
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