کد مقاله | کد نشریه | سال انتشار | مقاله انگلیسی | نسخه تمام متن |
---|---|---|---|---|
154722 | 456852 | 2015 | 10 صفحه PDF | دانلود رایگان |

• 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.
Journal: Chemical Engineering Science - Volume 135, 2 October 2015, Pages 393–402