Article ID | Journal | Published Year | Pages | File Type |
---|---|---|---|---|
226890 | Journal of Industrial and Engineering Chemistry | 2015 | 5 Pages |
Abstract
The performance of multi-stage circulating fast fluidized bed membrane reformers (CFFBMRs) for production of ultraclean hydrogen is investigated in comparison to a single circulating fast fluidized bed membrane reformer (CFFBMR). The two-stage reformer configuration gives significant increase in the methane conversion of 27.46% and ultraclean hydrogen yield of 29.61% compared to the single CFFBMR. The concept of the multi-stage short reformers policy is introduced. Impressively, substantial increase of ultraclean hydrogen yield of 83.91% is achieved.
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Physical Sciences and Engineering
Chemical Engineering
Chemical Engineering (General)
Authors
M.E.E. Abashar,