Article ID Journal Published Year Pages File Type
154722 Chemical Engineering Science 2015 10 Pages PDF
Abstract

•Micro-scale methanol fuel processor with a radial flow design is modeled.•Two types of performance improvements over the baseline reactor are proposed and modeled.•By including fins in the reactor design, the numerical simulation predicts a 2.7× increase in performance.

A 3-D model is presented for a novel sub-watt packed bed reactor. The reactor uses an annular inlet flow combined with a radial flow packed bed reactor. The baseline reactor is compared to a reactor with multiple outlets and a reactor with 3 internal fins. Increasing the outlets from 1 to 4 may have improved flow distribution, but did not increase the performance. However, inserting fins allowed >99% methanol conversion with approximately 30 K decrease in temperature with same inlet flow.

Related Topics
Physical Sciences and Engineering Chemical Engineering Chemical Engineering (General)
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