Abstract
In this research the performance of a fluidized bed membrane reactor for high temperature
water gas shift and its long term stability was investigated to provide a proof-of-concept of the new
system at lab scale. A demonstration unit with a capacity of 1 Nm3/h of ultra-pure H2 was designed,
built and operated over 900 h of continuous work. Firstly, the performance of the membranes were
investigated at different inlet gas compositions and at different temperatures and H2 partial pressure
differences. The membranes showed very high H2 fluxes (3.89E 6 mol m 2 Pa 1 s 1 at 400 C
and 1 atm pressure difference) with a H2/N2 ideal perm-selectivity (up to 21,000 when integrating
five membranes in the module) beyond the DOE 2015 targets. Monitoring the performance of the
membranes and the reactor confirmed a very stable performance of the unit for continuous high
temperature water gas shift under bubbling fluidization conditions. Several experiments were carried
out at different temperatures, pressures and various inlet compositions to determine the optimum
operating window for the reactor. The obtained results showed high hydrogen recovery factors,
and very low CO concentrations at the permeate side (in average <10 ppm), so that the produced
hydrogen can be directly fed to a low temperature PEM fuel cell.
Original language | English |
---|---|
Article number | 376 |
Journal | unknown |
Volume | unknown |
Issue number | 3 |
DOIs | |
Publication status | Published - 19 Mar 2016 |
Keywords
- fluidized bed membrane reactor
- water gas shift
- ultra-pure H2
- PEM fuel cell
- Ultra-pure H
Project and Funding Information
- Project ID
- info:eu-repo/grantAgreement/EC/FP7/262840/EU/Design and Manufacturing of Catalytic Membrane Reactors by developing new nano-architectured catalytic and selective membrane materials/DEMCAMER