Use of Pd-Ag Membrane Reactors for Low-Temperature Dry Reforming of Biogas-A Simulation Study.

Biogas is a valuable renewable energy source that can help mitigate greenhouse emissions. The dry reforming of methane (DRM) offers an alternative hydrogen production route with the advantage of using two main greenhouse gases, CO 2 and CH 4 . However, its real application is limited mainly due to catalyst deactivation by coke formation and the reverse water gas shift (RWGS) reaction that can occur in parallel. Additionally, the typical dry reforming temperature range is 700-950 °C, often leading to catalyst sintering. A low-temperature DRM process could be in principle achieved using a membrane reactor (MR) to shift the dry reforming equilibrium forward and inhibit the RWGS reaction. In this work, biogas reforming was investigated through the simulation of MRs with thin (3.4 µm) and thick (50 µm) Pd-Ag membranes. The effects of the feed temperature (from 450 to 550 °C), pressure (in the range of 2-20 bar), and biogas composition (CH 4 /CO 2 molar ratios from 1/1 to 7/3) were studied for the thin membrane through the calculation and comparison of several process indicators, namely CH 4 and CO 2 conversions, H 2 yield, H 2 /CO ratio and H 2 recovery. Estimation of the CO-inhibiting effect on the H 2 molar flux through the membrane was assessed for a thick membrane. Simulations for a thin Pd-Ag MR show that (i) CO 2 and CH 4 conversions and H 2 yield increase with the feed temperature; (ii) H 2 yield and average rate of coke formation increase for higher pressures; and (iii) increasing CH 4 /CO 2 feed molar ratio leads to higher H 2 /CO ratios, but lower H 2 yields. Moreover, simulations for a thick Pd-Ag MR showed that the average H 2 molar flux decreases due to the CO inhibiting effect ( ca . 15%) in the temperature range considered. In conclusion, this work showed that for the considered simulation conditions, the use of an MR leads to the inhibition of the RWGS reaction and improves H 2 yield, but coke formation and CO inhibition on H 2 permeation may pose limitations on its practical feasibility, for which proper strategies must be explored.