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Computational Fluid Dynamics Modeling of Thermally Integrated Microchannel Reforming Reactors for Hydrogen Production

Online Journal of Engineering Sciences | Vol 1, Issue 1

Figure 2

(a) Methanol conversion and (b) hydrogen production rate at different reaction temperatures. The experimental data [51, 52] are included for comparison.
Figure 2. (a) Methanol conversion and (b) hydrogen production rate at different reaction temperatures. The experimental data [51, 52] are included for comparison.