A catalytic hollow fibre membrane reactor for combined steam methane reforming and water gas shift reaction. (1st December 2015)

• Record Type: Journal Article
• Authors: Gouveia Gil, Ana; Wu, Zhentao; Chadwick, David; Li, K.
• Is Part Of: Chemical engineering science. Volume 137(2015)
• Page Start: 364
• Page End: 372
• Publication Date: 2015-12-01
• Subjects: Catalytic hollow fibre membrane reactor -- Steam methane reforming -- Water-gas shift -- H2 production -- Ni/SBA-15 catalyst -- Pd membrane; Chemical engineering -- Periodicals; Génie chimique -- Périodiques; Chemical engineering; Periodicals; Electronic journals; 660
• DOI: 10.1016/j.ces.2015.06.051
• Languages: English
• ISSNs: 0009-2509

Abstract

Abstract: A catalytic hollow fibre membrane reactor (CHFMR) was developed in this study for combined steam methane reforming (SMR) and water gas shift (WGS) reaction. This is achieved by incorporating a Ni/SBA-15 catalyst into a plurality of micro-channels with open entrance from inner surface of Al2 O3 hollow fibres, followed by coating of a 3.3 µm Pd membrane on the outer surface of the hollow fibre using an electroless plating method. In addition to systematic characterizations of each reactor component, i.e. Ni/SBA-15 catalyst, micro-structured ceramic hollow fibre and Pd separating layer, the effect of how the reactor was assembled or fabricated on the catalytic performance was evaluated. Electroless plating of the Pd membrane impaired the catalytic performance of the deposited Ni/SBA-15 catalyst. Also, the over-removal of hydrogen from the reaction zone was considered as the main reason for the deactivation of the Ni-based catalyst. Instead of mitigating such deactivation using "compensating" hydrogen, starting the reaction at higher temperatures was found more efficient in improving the reactor performance, due to a better match between hydrogen production (from the reaction) and hydrogen removal (from the Pd membrane). An effective methane conversion of approximately 53%, a CO2 selectivity of 94% and a H2 recovery of 43% can be achieved at 560 °C. In order for a more significant "shift" phenomenon, alternative methodology of fabricating the reactor and more coke resistant catalysts are recommended. Highlights: Match between H2 production and removal determines the performance of CHFMR. Pd membrane deposition can impair the catalyst performance inside the CHFMR. Over-removal of H2 from the reaction zone deactivates the Ni-based catalyst.