Development of H2 selective silica membranes: Performance evaluation through single gas permeation and gas separation tests

To prove the usefulness and achieve penetration of microporous ceramic membranes in gas separation applications of industrial interest, their behavior needs to be validated and predicted at relatively realistic conditions. In this respect, the present study employed hybrid silica (HybSi) membranes, modified by chemical vapor infiltration (CVI) in order to render them more selective to hydrogen in hydrogen/carbon dioxide binary mixtures, which are representative to effluent streams of methane or biogas steam reforming/water gas shift processes. Experimental studies with a single modified membrane exhibited high hydrogen permeance (1.5.10-7 mol.m(-2).s(-1).Pa-1, at 250 degrees C) and H-2/CO2 permselectivity (H-2/CO2 = 61.3, at 250 degrees C). Gas separation tests with binary gas mixtures revealed that high hydrogen purity values (>99%) can be reached at different process conditions. The mathematical model, also developed in this study in order to interpret the experimental results, can reliably predict hydrogen separation process performance over a wide range of operating conditions and also serve as a tool for subsequent optimum process engineering purposes.

Automated summary

This study utilized HybSi membranes modified by CVI to improve selectivity in hydrogen/carbon dioxide mixtures. Experimental results showed high hydrogen purity values could be achieved under various process conditions. The developed mathematical model can reliably predict hydrogen separation process performance and aid in optimization for process engineering purposes.